L-ornithine phenyl acetate and methods of making thereof

ABSTRACT

Disclosed herein are forms of L-ornithine phenyl acetate and methods of making the same. A crystalline form may, in some embodiments, be Forms I, II, III and V, or mixtures thereof. The crystalline forms may be formulated for treating subjects with liver disorders, such as hepatic encephalopathy. Accordingly, some embodiments include formulations and methods of administering L-ornithine phenyl acetate.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a divisional of U.S. application Ser. No. 12/753,763, filed Apr. 2, 2010, now U.S. Pat. No. 8,173,706, which claims the benefit of priority of U.S. Provisional Application No. 61/166,676, filed Apr. 3, 2009. The priority documents are hereby incorporated by reference in its entirety.

This application relates to PCT/US10/29708, filed Apr. 1, 2010, which was published in English as WO 2010/115055 A1 and designates the United States, and is hereby incorporated by reference in its entirety.

BACKGROUND

1. Field

The present application relates to the fields of pharmaceutical chemistry, biochemistry, and medicine. In particular, it relates to L-ornithine phenyl acetate salts and methods of making and using the same.

2. Description

Hyperammonemia is a hallmark of liver disease and is characterized by an excess of ammonia in the bloodstream. Hepatic encephalopathy is a primary clinical consequence of progressive hyperammonemia and is a complex neuropsychiatric syndrome, which may complicate acute or chronic hepatic failure. It is characterized by changes in mental state including a wide range of neuropsychiatric symptoms ranging from minor signs of altered brain function to overt psychiatric and/or neurological symptoms, or even deep coma. The accumulation of unmetabolized ammonia has been considered as the main factor involved in the pathogenesis of hepatic encephalopathy, but additional mechanisms may be associated.

L-Ornithine monohydrochloride and other L-ornithine salts are available for their use in the treatment of hyperammonemia and hepatic encephalopathy. For example, U.S. Publication No. 2008/0119554, which is hereby incorporated by reference in its entirety, describes compositions of L-ornithine and phenyl acetate for the treatment of hepatic encephalopathy. L-ornithine has been prepared by enzymatic conversion methods. For example, U.S. Pat. Nos. 5,405,761 and 5,591,613, both of which are hereby incorporated by reference in their entirety, describe enzymatic conversion of arginine to form L-ornithine salts. Sodium phenyl acetate is commercially available, and also available as an injectable solution for the treatment of acute hyperammonemia. The injectable solution is marketed as AMMONUL.

Although salt forms may exhibit improved degradation properties, certain salts, particularly sodium or chloride salts, may be undesirable when treating patients having diseases associated with the liver disease, such as hepatic encephalopathy. For example, a high sodium intake may be dangerous for cirrhotic patients prone to ascites, fluid overload and electrolyte imbalances. Similarly, certain salts are difficult to administer intravenously because of an increased osmotic pressure, i.e., the solution is hypertonic. High concentrations of excess salt may require diluting large volumes of solution for intravenous administration which, in turn, leads to excessive fluid overload. Accordingly, there exists a need for the preparation of L-ornithine and phenyl acetate salts which are favorable for the treatment of hepatic encephalopathy or other conditions where fluid overload and electrolyte imbalance are prevalent.

SUMMARY

Some embodiments disclosed herein include a composition comprising a crystalline form of L-ornithine phenyl acetate.

In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least three characteristic peaks, wherein said characteristic peaks are selected from the group consisting of approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising characteristic peaks at approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ.

In some embodiments, the crystalline form has a melting point of about 202° C. In some embodiments, the crystalline form exhibits a single crystal X-ray crystallographic analysis with crystal parameters approximately equal to the following: unit cell dimensions: a=6.594(2) Å, b=6.5448(18) Å, c=31.632(8) Å, α=90°, β=91.12(3)°, γ=90°; Crystal System: Monoclinic; and Space Group: P2₁. In some embodiments, the crystalline form is represented by the formula [C₅H₁₃N₂O₂][C₈H₇O₂].

Some embodiments have the crystalline form exhibit an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 4.9°, 13.2°, 17.4°, 20.8° and 24.4° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least three characteristic peaks, wherein said characteristic peaks are selected from the group consisting of approximately 4.9°, 13.2°, 17.4°, 20.8° and 24.4° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising characteristic peaks at approximately 4.9°, 13.2°, 17.4°, 20.8° and 24.4° 2θ.

Some embodiments have the crystalline form comprising water and/or ethanol molecules. In some embodiments, the crystalline form comprises about 11% by weight of said molecules as determined by thermogravimetric analysis. In some embodiments, the crystalline form is characterized by differential scanning calorimetry as comprising an endotherm at about 35° C. In some embodiments, the crystalline has a melting point at about 203° C.

Some embodiments have the crystalline form exhibiting a single crystal X-ray crystallographic analysis with crystal parameters approximately equal to the following: unit cell dimensions: a=5.3652(4) Å, b=7.7136(6) Å, c=20.9602(18) Å, α=90°, β=94.986(6)°, γ=90°; Crystal System: Monoclinic; and Space Group: P2₁. In some embodiments, the crystalline form is represented by the formula [C₅H₁₃N₂O₂][C₈H₇O₂]EtOH.H₂O.

Some embodiments have the crystalline form exhibiting an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least three characteristic peaks, wherein said characteristic peaks are selected from the group consisting of approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising characteristic peaks at approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ.

In some embodiments, the crystalline form is characterized by differential scanning calorimetry as comprising an endotherm at about 40° C. In some embodiments, the crystalline form comprises a melting point at about 203° C.

In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising at least three characteristic peaks, wherein said characteristic peak is selected from the group consisting of approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ. In some embodiments, the crystalline form exhibits an X-ray powder diffraction pattern comprising characteristic peaks at approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ.

In some embodiments, the crystalline form is characterized by differential scanning calorimetry as comprising an endotherm at about 174° C. In some embodiments, the crystalline form has a melting point of about 196° C. In some embodiments, the crystalline form comprises a pharmaceutically acceptable carrier.

Some embodiments disclosed herein have a composition comprising: at least about 50% by weight of a crystalline form of L-ornithine phenyl acetate salt and at least about 0.01% by weight benzoic acid or a salt thereof.

In some embodiments, the composition comprises at least about 0.10% by weight benzoic acid or a salt thereof. In some embodiments, the composition comprises no more than 5% by weight benzoic acid or a salt thereof. In some embodiments, the composition comprises no more than 1% by weight benzoic acid or a salt thereof.

In some embodiments, the composition further comprises at least 10 ppm silver. In some embodiments, comprises at least 20 ppm silver. In some embodiments, the composition further comprises at least 25 ppm silver. In some embodiments, comprises no more than 600 ppm silver. In some embodiments, composition comprises no more than 100 ppm silver. In some embodiments, the composition comprises no more than 65 ppm silver.

In some embodiments, about 50 mg/mL of the composition in water is isotonic with body fluids. In some embodiments, the isotonic solution has an osmolality in the range of about 280 to about 330 mOsm/kg.

In some embodiments, the composition has a density in the range of about 1.1 to about 1.3 kg/m³.

Some embodiments disclosed herein include a process for making L-ornithine phenyl acetate salt comprising: intermixing an L-ornithine salt, a benzoate salt and a solvent to form an intermediate solution; intermixing phenyl acetate with said intermediate solution; and isolating a composition comprising at least 70% crystalline L-ornithine phenyl acetate by weight.

In some embodiments, the process comprises removing at least a portion of a salt from said intermediate solution before intermixing the phenyl acetate, wherein said salt is not an L-ornithine salt. In some embodiments, the process comprises adding hydrochloric acid before removing at least a portion of the salt.

In some embodiments, intermixing the L-ornithine, the benzoate salt and the solvent comprises: dispersing the L-ornithine salt in water to form a first solution; dispersing the benzoate salt in DMSO to form a second solution; and intermixing said first solution and said second solution to form said solution.

In some embodiments, the composition comprises at least about 0.10% by weight benzoate salt. In some embodiments, composition comprises no more than 5% by weight benzoate salt. In some embodiments, composition comprises no more than 1% by weight benzoate salt.

In some embodiments, the L-ornithine salt is L-ornithine hydrochloride. In some embodiments, the benzoate salt is silver benzoate.

In some embodiments, the composition comprises at least 10 ppm silver. In some embodiments, composition comprises at least 20 ppm silver. In some embodiments, the composition comprises at least 25 ppm silver. In some embodiments, the composition comprises no more than 600 ppm silver. In some embodiments, the composition comprises no more than 100 ppm silver. In some embodiments, the composition comprises no more than 65 ppm silver.

In some embodiments, the phenyl acetate is in an alkali metal salt. In some embodiments, the alkali metal salt is sodium phenyl acetate.

In some embodiments, the composition comprises no more than 100 ppm sodium. In some embodiments, the composition comprises no more than 20 ppm sodium.

In some embodiments, the L-ornithine is in a halide salt. In some embodiments, the halide salt is L-ornithine hydrochloride.

In some embodiments, the composition comprises no more than 0.1% by weight chloride. In some embodiments, the composition comprises no more than 0.01% by weight chloride.

Some embodiments disclosed herein include a composition obtained by any of the processes disclosed herein.

Some embodiments disclosed herein include a process for making L-ornithine phenyl acetate salt comprising: increasing the pH value of a solution comprising an L-ornithine salt at least until an intermediate salt precipitates, wherein said intermediate salt is not an L-ornithine salt; isolating the intermediate salt from said solution; intermixing phenyl acetic acid with said solution; and isolating L-ornithine phenyl acetate salt from said solution.

In some embodiments, the pH value is increased to at least 8.0. In some embodiments, the pH value is increased to at least 9.0. In some embodiments, increasing the pH value comprises adding a pH modifier selected from the group consisting of sodium hydroxide, potassium hydroxide, sodium methoxide, potassium t-butoxide, sodium carbonate, calcium carbonate, dibutylamine, tryptamine, sodium hydride, calcium hydride, butyllithium, ethylmagnesium bromide or combinations thereof.

Some embodiments disclosed herein include a method of treating or ameliorating hyperammonemia in a subject by administering a therapeutically effective amount of a crystalline form of L-ornithine phenyl acetate salt.

In some embodiments, the crystalline form is administered orally.

In some embodiments, the crystalline form is selected from the group consisting of Form I, Form II, Form III, Form V, wherein: Form I exhibits an X-ray powder diffraction pattern having characteristic peaks at approximately 4.9°, 13.2°, 17.4°, 20.8° and 24.4° 2θ; Form II exhibits an X-ray powder diffraction pattern having characteristic peaks at approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ; Form III exhibits an X-ray powder diffraction pattern having characteristic peaks at approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ; and Form V exhibits an X-ray powder diffraction pattern having characteristic peaks at approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ.

In some embodiments, the crystalline form is Form I. In some embodiments, the crystalline form is Form II. In some embodiments, the crystalline form is Form III. In some embodiments, the crystalline form is Form V.

In some embodiments, the at least two crystalline forms selected from the group consisting of Form I, Form II, Form III and Form V, are administered. In some embodiments, the at least two crystalline forms are administered at about the same time.

In some embodiments, the crystalline form is administered from 1 to 3 times daily. In some embodiments, the therapeutically effective amount is in the range of about 500 mg to about 50 g.

In some embodiments, the subject is identified as having hepatic encephalopathy. In some embodiments, the subject is identified as having hyperammonemia.

Some embodiments disclosed herein include a process for making L-ornithine phenyl acetate salt comprising: intermixing an L-ornithine salt, silver phenyl acetate and a solvent to form a solution, wherein the L-ornithine salt is in halide salt; and isolating L-ornithine phenyl acetate from said solution.

Some embodiments disclosed herein include a method of treating or ameliorating hyperammonemia comprising intravenously administering a therapeutically effective amount of a solution comprising L-ornithine phenyl acetate, wherein said therapeutically effective amount comprises no more than 500 mL of said solution.

In some embodiments, the solution comprises at least about 25 mg/mL of L-ornithine phenyl acetate. In some embodiments, the solution comprises at least about 40 mg/mL of L-ornithine phenyl acetate. In some embodiments, the solution comprises no more than 300 mg/mL. In some embodiments, the solution is isotonic with body fluid.

Some embodiments disclosed herein include a method of compressing L-ornithine phenyl acetate, the method comprising applying pressure to a metastable form of L-ornithine phenyl acetate to induce a phase change.

In some embodiments, the metastable form is amorphous. In some embodiments, the metastable form exhibits an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 4.9°, 13.2°, 20.8° and 24.4° 2θ.

In some embodiments, the pressure is applied for a predetermined time. In some embodiments, the predetermined time is about 1 second or less. In some embodiments, the pressure is at least about 500 psi.

In some embodiments, the phase change yields a composition having a density in the range of about 1.1 to about 1.3 kg/m³ after applying the pressure.

In some embodiments, the phase change yields a composition exhibiting an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ.

Some embodiments disclosed herein include a composition obtained by applying pressure to a metastable form of L-ornithine phenyl acetate to induce a phase change.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is an X-ray powder diffraction pattern of Form I.

FIG. 2 shows differential scanning calorimetry results for Form I.

FIG. 3 shows thermogravimetric gravimetric/differential thermal analysis of Form I.

FIG. 4 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of Form I.

FIG. 5 shows dynamic vapor sorption results for Form I.

FIG. 6 is an X-ray powder diffraction pattern of Form II.

FIG. 7 shows differential scanning calorimetry results for Form II.

FIG. 8 shows thermogravimetric gravimetric/differential thermal analysis of Form II.

FIG. 9 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of Form II.

FIG. 10 shows dynamic vapor sorption results for Form II.

FIG. 11 is an X-ray powder diffraction pattern of Form III.

FIG. 12 shows differential scanning calorimetry results for Form III.

FIG. 13 shows thermogravimetric gravimetric/differential thermal analysis of Form III.

FIG. 14 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of Form III.

FIG. 15 shows dynamic vapor sorption results for Form III.

FIG. 16 is an X-ray powder diffraction pattern of Form V.

FIG. 17 shows differential scanning calorimetry results for Form V.

FIG. 18 shows thermogravimetric gravimetric/differential thermal analysis of Form V.

FIG. 19 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of Form V.

FIG. 20 shows dynamic vapor sorption results for Form V.

FIG. 21 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of L-ornithine benzoate.

FIG. 22 shows the ¹H nuclear magnetic resonance spectrum obtained from a sample of L-ornithine phenyl acetate.

DETAILED DESCRIPTION

Disclosed herein are methods of making L-ornithine phenyl acetate salts, and in particular, crystalline forms of said salt. These methods permit large-scale production of pharmaceutically acceptable forms of L-ornithine phenyl acetate using economical processes. Moreover, crystalline forms of L-ornithine phenyl acetate, including Forms I, II, III and V are also disclosed. The L-ornithine phenyl acetate salts permit intravenous administration with negligible concomitant sodium load, and therefore minimize the amount of i.v. fluid that is required.

The present application relates to new crystalline forms of L-ornithine phenyl acetate salts, as well as methods of making and using L-ornithine phenyl acetate salts. The salt advantageously exhibits long-term stability without significant amounts of sodium or chloride. As a result, L-ornithine phenyl acetate is expected to provide an improved safety profile compared to other salts of L-ornithine and phenyl acetate. Also, L-ornithine phenyl acetate exhibits lower tonicity compared to other salts, and therefore can be administered intravenously at higher concentrations. Accordingly, L-ornithine phenyl acetate is expected to provide significant clinical improvements for the treatment of hepatic encephalopathy.

The present application also relates to various polymorphs of L-ornithine phenyl acetate. The occurrence of different crystal forms (polymorphism) is a property of some molecules and molecular complexes. Salt complexes, such as L-ornithine phenyl acetate, may give rise to a variety of solids having distinct physical properties like melting point, X-ray diffraction pattern, infrared absorption fingerprint and NMR spectrum. The differences in the physical properties of polymorphs result from the orientation and intermolecular interactions of adjacent molecules (complexes) in the bulk solid. Accordingly, polymorphs can be distinct solids sharing the same active pharmaceutical ingredient yet having distinct advantageous and/or disadvantageous physico-chemical properties compared to other forms in the polymorph family.

Method of Making L-Ornithine Phenyl Acetate Salt

Some embodiments disclosed herein include a method of making L-ornithine phenyl acetate salt. L-Ornithine phenyl acetate may be produced, for example, through an intermediate salt, such as L-ornithine benzoate. As shown in Scheme 1, an L-ornithine salt of Formula I can be reacted with a benzoate salt of Formula II to obtain the intermediate L-ornithine benzoate.

Various salts of L-ornithine may be used in the compound of Formula I, and therefore X in Formula I can be any ion capable of forming a salt with L-ornithine other than benzoic acid or phenyl acetic acid. X can be a monoatomic anion, such as, but not limited to, a halide (e.g., fluoride, chloride, bromide, and iodide). X can also be a polyatomic anion, such as, but not limited to, acetate, aspartate, formate, oxalate, bicarbonate, carbonate, bitrate, sulfate, nitrate, isonicotinate, salicylate, citrate, tartrate, pantothenate, bitartrate, ascorbate, succinate, maleate, gentisinate, fumarate, gluconate, glucaronate, saccharate, formate, glutamate, methanesulfonate, ethanesulfonate, benzensulfonate, p-toluenesulfonate, pamoate (i.e., 1,1′-methylene-bis-(2-hydroxy-3-naphthoate), phosphate and the like. In some embodiments, X is a monovalent ion. In some embodiments, X is chloride.

Similarly, the benzoate salt of Formula II is not particularly limited, and therefore Y in Formula II can be any appropriate ion capable of forming a salt with benzoic acid. In some embodiments, Y can be a monoatomic cation, such as an alkali metal ion (e.g., Li⁺, Na⁺, and K⁺) and other monovalent ions (e.g., Ag⁺). Y may also be a polyatomic cation, such as ammonium, L-arginine, diethylamine, choline, ethanolamine, 1H-imidazole, trolamine, and the like. In some embodiments, Y is an inorganic ion. In some embodiments, Y is silver.

Many other possible salts of L-ornithine and benzoic acid may be used for the compounds of Formulae I and II, respectively, and can readily be prepared by those skilled in the art. See, for example, Bighley L. D., et al., “Salt forms of drugs and absorption,” In: Swarbrick J., Horlan J. C., eds. Encyclopedia of pharmaceutical technology, Vol. 12. New York: Marcel Dekker, Inc. pp. 452-499, which is hereby incorporated by reference in its entirety.

The intermediate L-ornithine benzoate (i.e., Formula III) can be prepared by intermixing solutions including compounds of Formulae I and II. As an example, the compounds of Formulae I and II may be separately dissolved in water and dimethyl sulfoxide (DMSO), respectively. The two solutions may then be intermixed so that the L-ornithine and benzoic acid react to form the salt of Formula III. Alternatively, the two salt compounds can be directly dissolved into a single solution. In some embodiments, L-ornithine and benzoic acid are dissolved in separate solvents, and subsequently intermixed. In some embodiments, L-ornithine is dissolved in an aqueous solution, benzoic acid is dissolved in an organic solvent, and the L-ornithine and benzoic acid solutions are subsequently intermixed.

Non-limiting examples of solvents which may be used when intermixing L-ornithine and benzoate salts include acetonitrile, dimethylsulfoxide (DMSO), cyclohexane, ethanol, acetone, acetic acid, 1-propanol, dimethylcarbonate, N-methyl-2-pyrrolidone (NMP), ethyl acetate (EtOAc), toluene, isopropyl alcohol (IPA), diisopropoyl ether, nitromethane, water, 1,4 dioxane, tdiethyl ether, ethylene glycol, methyl acetate (MeOAc), methanol, 2-butanol, cumene, ethyl formate, isobutyl acetate, 3-methyl-1-butanol, anisole, and combinations thereof. In some embodiments, the L-ornithine benzoate solution includes water. In some embodiments, the L-ornithine benzoate solution includes DMSO.

Upon intermixing L-ornithine and benzoate salts, counterions X and Y may form a precipitate that can be removed from the intermixed solution using known methods, such as filtration, centrifugation, and the like. In some embodiments, X is chloride, Y is silver, and the reaction produces a precipitate having AgCl. Although Scheme 1 shows the compounds of Formulae I and II as salts, it is also within the scope of the present application to intermix the free base of L-ornithine and benzoic acid to form the intermediate of L-ornithine benzoate. Consequently, forming and isolating the precipitate is optional.

The relative amount of L-ornithine and benzoate salts that are intermixed is not limited; however the molar ratio of L-ornithine to benzoic acid may optionally be in the range of about 10:90 and 90:10. In some embodiments, the molar ratio of L-ornithine benzoate can be in the range of about 30:70 and 30:70. In some embodiments, the molar ratio of L-ornithine to benzoate can be in the range of about 40:60 and 60:40. In some embodiments, the molar ratio of L-ornithine to benzoate is about 1:1.

In embodiments where X and Y are both inorganic ions (e.g., X and Y are chloride and silver, respectively), additional amounts of X-containing salt may be added to encourage further precipitation of the counterion Y. For example, if X is chloride and Y is silver, the molar ratio of L-ornithine hydrochloride to silver benzoate may be greater than 1:1 so that an excess of chloride is present relative to silver. Accordingly, in some embodiments, the molar ratio of L-ornithine to benzoic acid is greater than about 1:1. Nevertheless, the additional chloride salt is not required to be derived from an L-ornithine salt (e.g., L-ornithine hydrochloride). For example, dilute solutions of hydrochloric acid may be added to the solution to further remove silver. Although it is not particularly limited when the additional X-containing salt is added, it is preferably added before the AgCl is initially isolated.

As shown in Scheme 2, the L-ornithine benzoate can be reacted with a phenyl acetate salt of Formula IV to form L-ornithine phenyl acetate. For example, sodium phenyl acetate can be intermixed with a solution of L-ornithine benzoate to form L-ornithine phenyl acetate. Various salts of phenyl acetate may be used, and therefore Z in Formula IV can be any cation capable of forming a salt with phenyl acetate other than benzoic acid or L-ornithine. In some embodiments, Z can be a monoatomic cation, such as an alkali metal ion (e.g., Li⁺, Na⁺, and K⁺) and other monovalent ions (e.g., Ag⁺). Z may also be a polyatomic cation, such as ammonium, L-arginine, diethylamine, choline, ethanolamine, 1H-imidazole, trolamine, and the like. In some embodiments, Z is an inorganic ion. In some embodiments, Z is sodium.

The relative amount of L-ornithine and phenyl acetate salts that are intermixed is also not limited; however the molar ratio of L-ornithine to phenyl acetate may optionally be in the range of about 10:90 and 90:10. In some embodiments, the molar ratio of L-ornithine to phenyl acetate can be in the range of about 30:70 and 30:70. In some embodiments, the molar ratio of L-ornithine to phenyl acetate can be in the range of about 40:60 and 60:40. In some embodiments, the molar ratio of L-ornithine to benzoic acid is about 1:1.

The L-ornithine phenyl acetate of Formula V may then be isolated from solution using known techniques. For example, by evaporating any solvent until the L-ornithine phenyl acetate crystallizes, or alternatively by the adding an anti-solvent miscible in the L-ornithine phenyl acetate solution until the L-ornithine phenyl acetate precipitates from solution. Another possible means for isolating the L-ornithine phenyl acetate is to adjust the temperature of the solution (e.g., lower the temperature) until the L-ornithine phenyl acetate precipitates. As will be discussed in further detail in a later section, the method of isolating the L-ornithine phenyl acetate affects the crystalline form that is obtained.

The isolated L-ornithine phenyl acetate may be subjected to various additional processing, such as drying and the like. In some embodiments, L-ornithine phenyl acetate may be subsequently intermixed with a dilute HCl solution to precipitate residual silver. The L-ornithine phenyl acetate may again be isolated from solution using similar methods disclosed above.

As would be appreciated by a person of ordinary, guided by the teachings of the present application, L-ornithine phenyl acetate may similarly be prepared using an intermediate salt other than L-ornithine benzoate. Thus, for example, L-ornithine, or a salt thereof (e.g., L-ornithine hydrochloride), can be intermixed with a solution having acetic acid. L-Ornithine acetate may then be intermixed with phenyl acetic acid, or a salt thereof (e.g., sodium phenyl acetate), to obtain L-ornithine phenyl acetate. Scheme 4 illustrates an exemplary process of forming L-ornithine phenyl acetate using L-ornithine acetate as an intermediate salt. In some embodiments, the intermediate salt can be a pharmaceutically acceptable salt of L-ornithine. For example, the intermediate L-ornithine salt can be an acetate, aspartate, formate, oxalate, bicarbonate, carbonate, bitrate, sulfate, nitrate, isonicotinate, salicylate, citrate, tartrate, pantothenate, bitartrate, ascorbate, succinate, maleate, gentisinate, fumarate, gluconate, glucaronate, saccharate, formate, benzoate, glutamate, methanesulfonate, ethanesulfonate, benzensulfonate, p-toluenesulfonate, pamoate (i.e., 1,1′-methylene-bis-(2-hydroxy-3-naphthoate) or phosphate. The free acid of the intermediate is preferably a weaker acid relative to phenyl acetic acid. In some embodiments, the intermediate is an L-ornithine salt with an anion component that exhibits a pK_(a) value that is higher than the pK_(a) value of phenyl acetic acid. As an example, for L-ornithine acetate, acetic acid and phenyl acetic acid exhibit pK_(a) values of about 4.76 and 4.28, respectively.

L-Ornithine phenyl acetate may also be prepared, in some embodiments, without forming an intermediate salt, such as L-ornithine benzoate. Scheme 4 illustrates an exemplary process for preparing L-ornithine phenyl acetate without an intermediate salt. A pH modifier may be added to a solution of L-ornithine salt (e.g., as illustrated in Scheme 4 by the compound of Formula I) until a salt precipitates from solution, where the salt is not an L-ornithine salt. As an example, sodium methoxide (NaOMe) can be added to a solution of L-ornithine hydrochloride until sodium chloride precipitates from solution to leave a free base of L-ornithine. The precipitate may optionally be isolated from solution using known techniques, such as filtration, centrifugation, and the like. The free base of L-ornithine (e.g., as illustrated in Scheme 4 by the compound of Formula I-a) may be intermixed with phenyl acetic acid, or a salt thereof (e.g., as illustrated in Scheme 4 by the compound of Formula IV), to obtain L-ornithine phenyl acetate. The L-ornithine phenyl acetate of Formula V may then be isolated as previously described.

A pH modifier can include a basic compound, or anhydrous precursor thereof, and/or a chemically protected base. Non-limiting examples of pH modifiers include sodium hydroxide, potassium hydroxide, sodium methoxide, potassium t-butoxide, sodium carbonate, calcium carbonate, dibutylamine, tryptamine, sodium hydride, calcium hydride, butyllithium, ethylmagnesium bromide and combinations thereof. Also, the amount of pH modifier to be added is not particularly limited; however the molar ratio of L-ornithine to pH modifier may optionally be in the range of about 10:90 and 90:10. In some embodiments, the molar ratio of L-ornithine to pH modifier can be in the range of about 30:70 and 30:70. In some embodiments, the molar ratio of L-ornithine to pH modifier can be in the range of about 40:60 and 60:40. In some embodiments, the molar ratio of L-ornithine to pH modifier is about 1:1. The pH modifier may, in some embodiments be added to adjust the pH value to at least about 8.0; at least about 9.0; or at least about 9.5.

Another process for forming L-ornithine phenyl acetate, in some embodiments, includes reacting an alkali metal salt of L-ornithine with a phenyl acetate salt. As an example, L-ornithine hydrochloride may be intermixed with silver phenyl acetate and a solvent. AgCl may then precipitate and is optionally isolated from the solution. The remaining L-ornithine phenyl acetate can also be isolated using known methods. This process can be completed using generally the same procedures and conditions outlined above. For example, the relative molar amounts of L-ornithine to phenyl acetate can be 10:90 to 90:10; 30:70 to 70:30; 40:60 to 60:40; or about 1:1. Also, the L-ornithine phenyl acetate may be isolated by evaporating the solvent, adding an anti-solvent, and/or reducing the temperature.

Compositions of L-Ornithine Phenyl Acetate

Also disclosed herein are compositions of L-ornithine phenyl acetate. The compositions of the present application advantageously have low amounts of inorganic salts, particularly alkali metal salts and/or halide salts, and therefore are particularly suited for oral and/or intravenous administration to patients with hepatic encephalopathy. Meanwhile, these compositions may exhibit similar stability profiles compared to other salts (e.g., mixtures of L-ornithine hydrochloride and sodium phenyl acetate). The compositions may, in some embodiments, be obtained by one of the processes disclosed in the present application. For example, any of the disclosed processes using L-ornithine benzoate as an intermediate may yield the compositions of the present application.

The compositions, in some embodiments, can include a crystalline form of L-ornithine phenyl acetate (e.g., Forms I, II, III and/or V disclosed herein). In some embodiments, the composition may include at least about 20% by weight of a crystalline form of L-ornithine phenyl acetate (preferably at least about 50% by weight, and more preferably at least about 80% by weight). In some embodiments, the composition consists essentially of a crystalline form of L-ornithine phenyl acetate. In some embodiments, the composition includes a mixture of at least two (e.g., two, three or four forms) of Forms I, II, III, and V.

The compositions, in some embodiments, include Form II. For example, the compositions may include at least about 20%; at least about 50%; at least about 90%; at least about 95%; or at least about 99% of Form II. Similarly, the compositions may also include, for example, Forms I, III or V. The compositions may optionally include at least about 20%; at least about 50%; at least about 90%; at least about 95%; or at least about 99% of Forms I, II, III and/or V.

Also within the scope of the present application are amorphous forms of L-ornithine phenyl acetate. Various methods are known in the art for preparing amorphous forms. For example, a solution of L-ornithine phenyl acetate may be dried under vacuum by lyophilization to obtain an amorphous composition. See P.C.T. Application WO 2007/058634, which published in English and designates the U.S., and is hereby incorporated by reference for disclosing methods of lyophilization.

It is preferred that the composition have low amounts (if any) of alkali and halogen ions or salts, particular sodium and chloride. In some embodiments, the composition comprises no more than about 100 ppm of alkali metals (preferably no more than about 20 ppm, and most preferably no more than about 10 ppm). In some embodiments, the composition comprises no more than about 100 ppm of sodium (preferably no more than about 20 ppm, and most preferably no more than about 10 ppm). In some embodiments, the composition comprises no more than about 0.1% by weight of halides (preferably no more than about 0.01% by weight). In some embodiments, the composition comprises no more than about 0.1% by weight of chloride (preferably no more than about 0.01% by weight).

The reduced content of alkali metals and halides provides a composition suitable for preparing concentrated isotonic solutions. As such, these compositions can be more easily administered intravenously compared to, for example, administering mixtures of L-ornithine hydrochloride and sodium phenyl acetate. In some embodiments, an about 45 to about 55 mg/mL solution of L-ornithine phenyl acetate in water (preferably about 50 mg/mL) is isotonic with body fluids (e.g., the solution exhibits an osmolality in the range of about 280 to about 330 mOsm/kg).

The compositions may also include residual amounts of the anion from an intermediate salt formed during the process of making the L-ornithine phenyl acetate composition. For example, some of the processes disclosed herein yield compositions having benzoic acid or a salt thereof. In some embodiments, the composition comprises at least about 0.01% by weight benzoic acid or a salt thereof (preferably at least about 0.05% by weight, and more preferably about 0.1% by weight). In some embodiments, the composition comprises no more than about 3% by weight benzoic acid or a salt thereof (preferably no more than about 1% by weight, and more preferably no more than about 0.5% by weight). In some embodiments, the composition includes a salt, or an acid thereof, in the range of about 0.01% to about 3% by weight (preferably about 0.1% to about 1%), wherein the salt is selected from acetate, aspartate, formate, oxalate, bicarbonate, carbonate, bitrate, sulfate, nitrate, isonicotinate, salicylate, citrate, tartrate, pantothenate, bitartrate, ascorbate, succinate, maleate, gentisinate, fumarate, gluconate, glucaronate, saccharate, formate, benzoate, glutamate, methanesulfonate, ethanesulfonate, benzensulfonate, p-toluenesulfonate, pamoate (i.e., 1,1′-methylene-bis-(2-hydroxy-3-naphtho ate) or phosphate.

Similarly, a composition prepared using an acetate intermediate may have residual amounts of acetic acid or acetate. In some embodiments, the composition includes at least about 0.01% by weight acetic acid or acetate (preferably at least about 0.05% by weight, and more preferably about 0.1% by weight). In some embodiments, the composition includes no more than about 3% by weight acetic acid or acetate (preferably no more than about 1% by weight, and more preferably no more than about 0.5% by weight).

The compositions may also include low amounts of silver. Exemplary processes disclosed herein utilize, for example, silver benzoate, but still yield compositions with surprisingly low amounts of silver. Thus, in some embodiments, the composition includes no more than about 600 ppm silver (preferably no more than about 100 ppm, and more preferably no more than about 65 ppm). In some embodiments, the composition includes at least about 10 ppm silver (alternatively at least about 20 or 25 ppm silver).

Pharmaceutical Compositions

The compositions of L-ornithine phenyl acetate of the present application may also be formulated for administration to a subject (e.g., a human). L-Ornithine phenyl acetate, and accordingly the compositions disclosed herein, may be formulated for administration with a pharmaceutically acceptable carrier or diluent. L-ornithine phenyl acetate may thus be formulated as a medicament with a standard pharmaceutically acceptable carrier(s) and/or excipient(s) as is routine in the pharmaceutical art. The exact nature of the formulation will depend upon several factors including the desired route of administration. Typically, L-ornithine phenyl acetate is formulated for oral, intravenous, intragastric, subcutaneous, intravascular or intraperitoneal administration.

The pharmaceutical carrier or diluent may be, for example, water or an isotonic solution, such as 5% dextrose in water or normal saline. Solid oral forms may contain, together with the active compound, diluents, e.g. lactose, dextrose, saccharose, cellulose, corn starch or potato starch; lubricants, e.g. silica, talc, stearic acid, magnesium or calcium stearate, and/or polyethylene glycols; binding agents, e.g. starches, gum arabic, gelatin, methylcellulose, carboxymethylcellulose or polyvinyl pyrrolidone; disaggregating agents, e.g. starch, alginic acid, alginates or sodium starch glycolate; effervescing mixtures; dyestuffs; sweeteners; wetting agents, such as lecithin, polysorbates, laurylsulphates; and, in general, non-toxic and pharmacologically inactive substances used in pharmaceutical formulations. Such pharmaceutical preparations may be manufactured in known manners, for example, by means of mixing, granulating, tabletting, sugar-coating, or film-coating processes.

Liquid dispersions for oral administration may be syrups, emulsions or suspensions. The syrups may contain as carriers, for example, saccharose or saccharose with glycerine and/or mannitol and/or sorbitol.

Suspensions and emulsions may contain a carrier, for example a natural gum, agar, sodium alginate, pectin, methylcellulose, carboxymethylcellulose, or polyvinyl alcohol. The suspensions or solutions for intramuscular injections may contain, together with L-ornithine phenyl acetate, a pharmaceutically acceptable carrier, e.g. sterile water, olive oil, ethyl oleate, glycols, e.g. propylene glycol, and if desired, a suitable amount of lidocaine hydrochloride.

The medicament may consist essentially of L-ornithine phenyl acetate and a pharmaceutically acceptable carrier. Such a medicament therefore contains substantially no other amino acids in addition to L-ornithine and phenyl acetate. Furthermore, such a medicament contains insubstantial amounts of other salts in addition to L-ornithine phenyl acetate.

Oral formulations may generally include dosages of L-ornithine phenyl acetate in the range of about 500 mg to about 100 g. Accordingly, in some embodiments, the oral formulation includes the L-ornithine phenyl acetate compositions disclosed herein in the range of about 500 mg to about 50 g. In some embodiments, the oral formulation is substantially free of alkali metal salts and halides (e.g., contains no more than trace amounts of alkali metal salts and halides).

Intravenous formulations may also generally include dosages of L-ornithine phenyl acetate in the range of about 500 mg to about 100 g (preferably about 1 g to about 50 g). In some embodiments, the intravenous formulation is substantially free of alkali metal salts and halides (e.g., contains no more than trace amounts of alkali metal salts and halides). In some embodiments, the intravenous formulation has a concentration of about 5 to about 300 mg/mL of L-ornithine phenyl acetate (preferably about 25 to about 200 mg/mL, and more preferably about 40 to about 60 mg/mL).

The composition, or medicament containing said composition, may optionally be placed is sealed packaging. The sealed packaging may reduce or prevent moisture and/or ambient air from contacting the composition or medicament. In some embodiments, the packaging includes a hermetic seal. In some embodiments, the packaging sealed under vacuum or with an inert gas (e.g., argon) within the sealed package. Accordingly, the packaging can inhibit or reduce the rate of degradation for the composition or medicament stored within the packaging. Various types of sealed packaging are known in the art. For example, U.S. Pat. No. 5,560,490, is hereby incorporate by reference in its entirety, discloses an exemplary sealed package for medicaments.

Compositions with Improved Density

Applicants have surprisingly found that compositions with greater density may be obtained by applying sufficient pressure to compositions having Form I (described below) to induce a transition to Form II (described below). For example, applying 3 tons of force for 90 minutes to Forms I and II yield densities of 1.197 kg/m³ and 1.001 kg/m³, respectively. Surprisingly, Form I converted to Form II under these conditions; therefore the greater density appears to be explained by the different crystalline form as the starting material.

Accordingly, disclosed herein are methods of increasing the density of an L-ornithine phenyl acetate composition having Form I by applying pressure to the composition sufficient to induce a transition to Form II. The appropriate amount of force or pressure to induce the phase change may vary with the amount of time the force or pressure is applied. Thus, a person of ordinary skill, guided by the teachings of the present application, can determine appropriate amounts of pressure and time to induce the phase change. In some embodiments, at least about 1 ton of force is applied (preferably at least about 2 tons, and more preferably about 3 tons). In some embodiments, at least about 500 psi of pressure is applied (preferably at least about 1000 psi, and more preferably at least about 2000 psi).

The amount of time for applying pressure is not particularly limited, and as discussed above, will vary depending upon the amount time. For example, when applying large forces (e.g., 10 tons) to a typical tablet-sized punch, the time may be about 1 second or less. In some embodiments, the time for apply pressure is a predetermined time. The time may be, for example, about 0.1 seconds; about 1 second; at least about 1 minute; at least about 5 minutes; or at least about 20 minutes.

In some embodiments, the composition includes at least about 10% by weight of Form I. In some embodiments, the composition includes at least about 30% by weight of Form I.

Without being bound to any particular theory, Applicants believe the greater density may result, at least in part, from ethanol solvate component present in Form I. Applying pressure to the solvate may facilitate forming a denser structure with fewer defects (e.g., grain boundaries). Consequently, in some embodiments, methods of increasing the density of an L-ornithine phenyl acetate composition having solvate components include applying pressure to the composition sufficient to induce a transition to Form II. In some embodiments, the pressure is at least about 500 psi (preferably at least about 1000 psi, and more preferably at least about 2000 psi). In some embodiments, the time for apply pressure is a predetermined time. In some embodiments, the composition includes at least about 10% of the solvate form (preferably at least about 30%, and more preferably at least about 50%).

The compositions of L-ornithine phenyl acetate disclosed herein may therefore have higher densities compared to compositions obtain by, for example, precipitating a crystalline form. In some embodiments, the composition has a density of at least about 1.1 kg/m³ (preferably at least about 1.15 kg/m³, and more preferably at least about 1.18 kg/m³). In some embodiments, the composition has a density of no more than about 1.3 kg/m³ (preferably no more than about 1.25 kg/m³, and more preferably no more than about 1.22 kg/m³). In some embodiments, the composition has a density of about 1.2 kg/m³.

Crystalline Forms of L-Ornithine Phenyl Acetate

Also disclosed herein are crystalline forms of L-ornithine phenyl acetate, and in particular, crystalline Form I, Form II, Form III, and Form V. L-Ornithine phenyl acetate may, in some embodiments, be obtained using the processes disclosed above and then crystallized using any of the methods disclosed herein.

Form I

The precise conditions for forming crystalline Form I may be empirically determined and it is only possible to give a number of methods which have been found to be suitable in practice.

Thus, for example, crystalline Form I may generally be obtained by crystallizing L-ornithine phenyl acetate under controlled conditions. As an example, precipitating L-ornithine phenyl acetate from a saturated solution by adding ethanol at reduced temperatures (e.g., 4° or −21° C.). Exemplary solvents for the solution that yield crystalline Form I upon adding ethanol include, but are not limited to, cyclohexanone, 1-propanol, diemthylcarbonate, N-methylpyrrolidine (NMP), diethyl ether, 2-butanol, cumene, ethyl formate, isobutyl acetate, 3-nethyl-1-butanol, and anisole.

Accordingly, in the context of the processes for making L-ornithine phenyl acetate disclosed above, the process can yield Form I by utilizing particular isolation methods. For example, L-ornithine phenyl acetate may be isolated by adding ethanol at reduced temperature to yield Form I.

Crystalline Form I was characterized using various techniques which are described in further detail in the experimental methods section. FIG. 1 shows the crystalline structure of Form I as determined by X-ray powder diffraction (XRPD). Form I, which may be obtained by the methods disclosed above, exhibits characteristic peaks at approximately 4.9°, 13.2°, 17.4°, 20.8° and 24.4° 2θ. Thus, in some embodiments, a crystalline form of L-ornithine phenyl acetate has one or more characteristic peaks (e.g., one, two, three, four or five characteristic peaks) selected from approximately 4.9°, 13.2°, 17.4°, 20.8°, and 24.4° 2θ.

As is well understood in the art, because of the experimental variability when X-ray diffraction patterns are measured on different instruments, the peak positions are assumed to be equal if the two theta (2θ) values agree to within 0.2° (i.e., ±0.2°). For example, the United States Pharmacopeia states that if the angular setting of the 10 strongest diffraction peaks agree to within ±0.2° with that of a reference material, and the relative intensities of the peaks do not vary by more than 20%, the identity is confirmed. Accordingly, peak positions within 0.2° of the positions recited herein are assumed to be identical.

FIG. 2 shows results obtained by differential scanning calorimetry (DSC) for Form I. These results indicate an endotherm at 35° C., which is possibly associated with a desolvation and/or dehydration to Form II. A second transition at about 203° C. indicates the melting point for the crystal. To explore the possible existence of a desolvation and/or dehydration transition, Form I was analyzed by thermogravimetric gravimetric/differential thermal analysis (TG/DTA), which is shown in FIG. 3. Form I exhibits a 11.28% weight loss at about 35° C., and therefore these results further suggest that Form I exhibits a desolvation and/or dehydration transition at about 35° C. The melting point of about 203° C. could also be observed by TGA testing. Accordingly, in some embodiments, the crystalline form of L-ornithine phenyl acetate is characterized by differential scanning calorimetry as having an endotherm at about at about 35° C. In some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a weight loss of about 11% at about 35° C., as determined by TGA. In some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a melting point of about 203° C.

FIG. 4 shows nuclear magnetic resonance (NMR) integrals and chemical shifts for Form I. The integrals confirm the presence of L-ornithine phenyl acetate: 7.5 (aromatic CH), 3.8 (CH adjacent to NH₂), 3.6 (CH₂ unit of phenyl acetate), 3.15 (CH₂ adjacent to NH₂) and 1.9 (aliphatic CH₂ units) ppm (integrals: 5:1:2:2:4 protons; 1.2, 0.25, 0.5, 0.5, 1.0). Amine protons and hydroxyl protons were not observed due to proton exchange at both the zwitterion and site of salt formation. Meanwhile, FIG. 5 shows dynamic vapor sorption (DVS) results for Form I, and show a water uptake of about 0.2% by weight. XRPD results following DVA analysis (not shown) confirm that Form I did not transition to a different polymorph. Form I can therefore be characterized as non-hygroscopic and stable over a wide range of humidity.

A 7-day stability study of Form I at 40° C./75% RH indicated that a transformation to Form II occurred under these conditions. Form I also converts to Form II at elevated temperatures (e.g., 80° or 120° C.), with or without applying a vacuum, after 7 or 14 days. Accordingly, Form I is metastable.

Single crystal x-ray diffraction (SXRD) was also used to determine the structure of Form I at −20° and −123° C., and the results are summarized in TABLES 1 and 2. The results confirm that Form I is a solvate having ethanol and water molecules within the unit cell. In some embodiments, a crystalline form of L-ornithine phenyl acetate can be represented by the formula C₁₅H₂₈N₂O₆. In some embodiments, a crystalline form of L-ornithine phenyl acetate can be represented by the formula [C₅H₁₃N₂O₂][C₈H₇O₂]EtOH.H₂O. In some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a single crystal X-ray crystallographic analysis with crystal parameters approximately equal to the following: unit cell dimensions of a=5.3652(4) Å, b=7.7136(6) Å, c=20.9602(18) Å, α=90°, β=94.986(6)°, γ=90°; a monoclinic crystal system, and a P2₁ space group.

TABLE 1 Crystallographic Data of Form I Collected at −20° C. Empirical Formula C₁₅H₂₈N₂O₆ or [C₅H₁₃N₂O₂][C₈H₇O₂]EtOH•H₂O Formula Weight 332.39 Crystal System Monoclinic Space Group P2₁ Unit Cell Dimensions a = 5.3652(4) Å α = 90° b = 7.7136(6) Å β = 94.986(6)° c = 20.9602(18) Å γ = 90° Volume 864.16(12) Å³ Number of Reflections 1516 (2.5° < θ < 28°) Density (calculated) 1.277 mg/cm³

TABLE 2 Crystallographic Data of Form I Collected at −123° C. Empirical Formula C₁₅H₂₈N₂O₆ or [C₅H₁₃N₂O₂][C₈H₇O₂]EtOH•H₂O Formula Weight 332.39 Crystal System Monoclinic Space Group P2₁ Unit Cell Dimensions a = 5.3840(9) Å α = 90° b = 7.7460(12) Å β = 95.050(12)° c = 21.104(4) Å γ = 90° Volume 876.7(3) Å³ Number of Reflections 1477 (2.5° < θ < 18°) Density (calculated) 1.259 mg/cm³ Form II

The precise conditions for forming crystalline Form II may be empirically determined and it is only possible to give a number of methods which have been found to be suitable in practice.

Thus, for example, crystalline Form II may be prepared by crystallization under controlled conditions. Crystalline Form II can be prepared by, for example, evaporating a saturated organic solution of L-ornithine phenyl acetate. Non-limiting examples of organic solutions that may be used to obtain Form II include ethanol, acetone, benzonitrile, dichloromethane (DCM), dimethyl sulfoxide (DMSO), ethyl acetate (EtOAc), acetonitrile (MeCN), methyl acetate (MeOAc), nitromethane, tert-butyl methyl ether (TBME), tetrahydrofuran, and toluene. Other solvents may yield a mixture of Form I and II, such as, but not limited to, 1,4 dioxane, 1-butanol, cyclohexane, IPA, TRF, MEK, MeOAc and water.

Form II can also be obtained by precipitating L-ornithine phenyl acetate from a saturated organic solution by adding an anti-solvent for L-ornithine phenyl acetate, such as IPA. Form II may be precipitated over a broad range of temperatures (e.g., room temperature, 4° C., and −21° C.). Non-limiting examples of suitable solvents for the saturated organic solution include cyclohexanone, 1-propanol, dimethyl carbonate, N-methylpyrrolidone (NMP), diisopropyl ether, diethyl ether, ethylene glycol, dimethylformamide (DMF), 2-butanol, cumene, isobutyl acetate, 3-methyl-1-butanol, and anisole. Alternatively, the same listed solvents (e.g., cyclohexanone) can be used to form a solution of L-ornithine phenyl acetate, and Form II may be precipitated by adding ethanol at ambient conditions. As another example, Form II may also be obtained by forming a slurry of L-ornithine phenyl acetate with the listed organic solvents and cycling the temperature between 25° and 40° C. every 4 hours for about 18 cycles (or 72 hours).

Accordingly, in the context of the processes for making L-ornithine phenyl acetate disclosed above, the process can yield Form II by utilizing particular isolation methods. For example, L-ornithine phenyl acetate may by isolated by adding IPA, or evaporating the organic solvent, to yield Form II.

FIG. 6 shows the crystalline structure of Form II as determined by XRPD. Form II, which may be obtained by the methods disclosed above, exhibits characteristic peaks at approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ. Thus, in some embodiments, a crystalline form of L-ornithine phenyl acetate has one or more characteristic peaks (e.g., one, two, three, four, five or six characteristic peaks) selected from approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.12° θ.

FIG. 7 shows results obtained by differential scanning calorimetry (DSC) for Form II. These results indicate a melting point of about 202° C., which is approximately the same as the melting point for Form I. This suggests that Form I transitions to Form II upon heating above about 35° C. Form II was also analyzed using TG/DTA, as shown in FIG. 8, and exhibits an about 9.7% weight loss associated with residual solvent. The melting point of about 202° C. could also be observed by TGA testing. Accordingly, in some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a melting point of about 202° C.

A 7-day stability study of Form II at 40° C./75% RH failed to produce an observable phase change. In fact, Form II was stable over 14 days when exposed to elevated temperatures, varying pHs, UV light or oxygen. Accordingly, Form II is considered stable.

FIG. 9 shows nuclear magnetic resonance (NMR) integrals and chemical shifts for Form II. The integrals confirm the presence of L-ornithine phenyl acetate: 7.5 (aromatic CH), 3.8 (CH adjacent to NH2), 3.6 (CH2 unit of phenylacetate), 3.15 (CH2 adjacent to NH2) and 1.9 (aliphatic CH2 units) ppm (integrals: 5:1:2:2:4 protons; 7.0, 1.4, 2.9, 3.0, 5.9). Amine protons and hydroxyl protons were not observed due to proton exchange at both the zwitterion and site of salt formation. Meanwhile, FIG. 10 shows dynamic vapor sorption (DVS) results for Form II, and show a water uptake of about 0.3% by weight. XRPD results following DVA analysis (not shown) confirm that Form II did not transition to a different polymorph. Form II can therefore be characterized as non-hygroscopic and stable over a wide range of humidity.

Single crystal x-ray diffraction (SXRD) was also used to determine the structure of Form II at 23° and −123° C., and the results are summarized in TABLES 3 and 4. The results demonstrate that Form II is anhydrous and therefore structurally different from Form I. In some embodiments, a crystalline form of L-ornithine phenyl acetate can be represented by the formula C₁₃H₂₀N₂O₄. In some embodiments, a crystalline form of L-ornithine phenyl acetate can be represented by the formula [C₅H₁₃N₂O₂][C₈H₇O₂]. In some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a single crystal X-ray crystallographic analysis with crystal parameters approximately equal to the following: unit cell dimensions of a=6.594(2) Å, α=90°, b=6.5448(18) Å, β=91.12(3)°, c=31.632(8) Å, γ=90°; a monoclinic crystal system; and a P2₁ space group.

TABLE 3 Crystallographic Data of Form II Collected at 23° C. Empirical Formula C₁₃H₂₀N₂O₄ or [C₅H₁₃N₂O₂][C₈H₇O₂] Formula Weight 268.31 Crystal System Monoclinic Space Group P2₁ Unit Cell Dimensions a = 6.594(2) Å α = 90° b = 6.5448(18) Å β = 91.12(3)° c = 31.632(8) Å γ = 90° Volume 1364.9(7) Å³ Number of Reflections 3890 (3° < θ < 20.5°) Density (calculated) 1.306 mg/cm³

TABLE 4 Crystallographic Data of Form II Collected at −123° C. Empirical Formula C₁₅H₂₈N₂O₆ or [C₅H₁₃N₂O₂][C₈H₇O₂] Formula Weight 332.39 Crystal System Monoclinic Space Group P2₁ Unit Cell Dimensions a = 5.3652(4) Å α = 90° b = 7.7136(6) Å β = 94.986(6)° c = 20.9602(18) Å γ = 90° Volume 864.16(12) Å³ Number of Reflections 1516 (2.5° < θ < 28°) Density (calculated) 1.277 mg/cm³ Form III

The precise conditions for forming crystalline Form III may be empirically determined and it is only possible to give a number of methods which have been found to be suitable in practice.

Thus, for example, Form III may be obtained by placing a saturated solution of L-ornithine phenyl acetate in a cooled temperature environment of about −21° C., where the solution is a mixture of acetone and water (e.g., equal parts volume of acetone and water). As another example, adding IPA to a saturated solution of L-ornithine phenyl acetate in 2-butanol can yield Form III when completed at ambient conditions. Furthermore, Form III may be obtained, for example, by adding IPA to a saturated solution of L-ornithine phenyl acetate in isobutyl acetate when completed at reduced temperatures of about −21° C.

Accordingly, in the context of the processes for making L-ornithine phenyl acetate disclosed above, the process can yield Form III by utilizing particular solvents and isolation methods. For example, L-ornithine phenyl acetate may be formed within a mixture of acetone and water, and subsequently placed in a cool environment of about −21° C. to yield Form III.

FIG. 11 shows the crystalline structure of Form III as determined by XRPD. Form III, which may be obtained by the methods disclosed above, exhibits characteristic peaks at approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ. Thus, in some embodiments, a crystalline form of L-ornithine phenyl acetate has one or more characteristic peaks (e.g., one, two, three, four, five or six characteristic peaks) selected from approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ.

FIG. 12 shows results obtained by differential scanning calorimetry (DSC) for Form III. These results indicate a melting point of about 203° C., which is approximately the same as the melting points for Form I and Form II. Additionally, Form III exhibits an endotherm at about 40° C. Form III was also analyzed using TG/DTA, as shown in FIG. 13, and exhibits no significant weight loss before the melting point. Form III may therefore be characterized as anhydrous. The melting point of about 203° C. could also be observed by TGA testing. Accordingly, in some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a melting point of about 203° C. In some embodiments, a crystalline form of L-ornithine phenyl acetate is characterized by differential scanning calorimetry as having an endotherm at about 40° C. In some embodiments, a crystalline form of L-ornithine phenyl acetate is anhydrous.

A 7-day stability study of Form III at 40° C./75% RH indicated that a transformation to Form II occurred under these conditions. In contrast, Form II is stable at elevated temperatures, with or without vacuum, for periods of 7 or 10 days. Accordingly, Form III is most likely metastable, but more stable than Form I.

FIG. 14 shows nuclear magnetic resonance (NMR) integrals and chemical shifts for Form III. The integrals confirm the presence of L-ornithine phenyl acetate: 7.5 (aromatic CH), 3.8 (CH adjacent to NH2), 3.6 (CH2 unit of phenyl acetate), 3.15 (CH2 adjacent to NH2) and 1.9 (aliphatic CH2 units) ppm (integrals: 5:1:2:2:4 protons; 4.2, 0.8, 1.7, 1.7, 3.0). Amine protons and hydroxyl protons were not observed due to proton exchange at both the zwitterion and site of salt formation. Meanwhile, FIG. 15 shows dynamic vapor sorption (DVS) results for Form III, and show a water uptake of about 2.0% by weight. XRPD results following DVS analysis (not shown) confirm that Form III did not transition to a different polymorph. Form III therefore exhibits greater water uptake compared to Forms I and II; however Form III is still characterized as non-hygroscopic and stable over a wide range of humidity at room temperature.

Form V

The precise conditions for forming crystalline Form V may be empirically determined and it is only possible to give a number of methods which have been found to be suitable in practice.

Thus, for example, Form V may be obtained by placing a saturated solution of L-ornithine phenyl acetate in a cooled temperature environment of about −21° C., where the solution is cyclohexanone. As another example, the same saturated solution may yield Form V when evaporating the solvent.

Form V also forms from saturated solutions of L-ornithine phenyl acetate having diisopropyl ether as a solvent. For example, a saturated solution having a solvent ratio of about 1 to 2 of diisopropyl ether and IPA will yield Form V when placed in a cooled temperature environment of about 4° C. Similarly, a solution having only the solvent diisopropyl ether can yield Form V when placed in a cooled temperature environment of about −21° C.

FIG. 16 shows the crystalline structure of Form V as determined by XRPD. Form V, which may be obtained by the methods disclosed above, exhibits characteristic peaks at approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ. Thus, in some embodiments, a crystalline form of L-ornithine phenyl acetate has one or more characteristic peaks (e.g., one, two, three, four, or five characteristic peaks) selected from approximately 13.7°, 17.4°, 19.8°, 20.6° and 23.7° 2θ.

FIG. 17 shows results obtained by differential scanning calorimetry (DSC) for Form V. These results indicate a melting point of about 196° C., which is below the melting point of other forms. Form V also exhibits an endotherm at about 174° C. Form V was also analyzed using thermal gravimetric analysis (TGA), as shown in FIG. 18, and exhibits no significant weight loss before the melting point. Form V may therefore be characterized as anhydrous. The melting point of about 196° C. could also be observed by TGA testing. Accordingly, in some embodiments, a crystalline form of L-ornithine phenyl acetate exhibits a melting point of about 196° C. In some embodiments, a crystalline form of L-ornithine phenyl acetate is characterized by differential scanning calorimetry as having an endotherm at about 174° C. In some embodiments, a crystalline form of L-ornithine phenyl acetate is anhydrous.

FIG. 19 shows nuclear magnetic resonance (NMR) integrals and chemical shifts for Form V. The integrals confirm the presence of L-ornithine phenyl acetate: 7.5 (aromatic CH), 3.8 (CH adjacent to NH2), 3.6 (CH2 unit of phenyl acetate), 3.15 (CH2 adjacent to NH2) and 1.9 (aliphatic CH2 units) ppm (integrals: 5:1:2:2:4 protons; 4.2, 0.8, 1.7, 1.7, 3.0). Amine protons and hydroxyl protons were not observed due to proton exchange at both the zwitterion and site of salt formation. Meanwhile, FIG. 19 shows dynamic vapor sorption (DVS) results for Form V, and show a water uptake of about 0.75% by weight. XRPD results following DVS analysis (not shown) suggest that Form V transitioned to Form II, but the chemical composition was unchanged. Form V is therefore characterized as non-hygroscopic, but not stable over a wide range of humidity.

A 7-day stability study of Form V at 40° C./75% RH indicated that a transformation to Form II occurred under these conditions; however the chemical composition was unchanged. Accordingly, Form V is most likely metastable.

Methods of Treating Liver Decompensation or Hepatic Encephalopathy

L-Ornithine phenyl acetate, and accordingly any of the compositions of L-ornithine phenyl acetate disclosed herein, may be administered to a subject for treating or ameliorating the onset of liver decompensation or hepatic encephalopathy. L-Ornithine phenyl acetate can thus be administered to improve the condition of a subject, for example a subject suffering from chronic liver disease following a precipitating event. As another example, L-ornithine phenyl acetate may be administered to combat or delay the onset of liver decompensation or hepatic encephalopathy.

L-Ornithine phenyl acetate may be administered in combination to a subject for treatment of hepatic encephalopathy. L-Ornithine phenyl acetate may be administered to improve the condition of a patient suffering from hepatic encephalopathy. L-Ornithine phenyl acetate may be administered to alleviate the symptoms associated with hepatic encephalopathy. L-Ornithine phenyl acetate may be administered to combat hepatic encephalopathy. L-Ornithine phenyl acetate may be administered to prevent or reduce the likelihood of an initial hepatic encephalopathic episode in a person at risk for hepatic encephalopathic episodes. L-Ornithine phenyl acetate may be administered to lessen the severity of an initial hepatic encephalopathic episode in a person at risk for hepatic encephalopathic episodes. L-Ornithine phenyl acetate may be administered to delay an initial hepatic encephalopathic episode in a person at risk for hepatic encephalopathic episodes.

Development of liver decompensation and hepatic encephalopathy commonly involves “precipitating events” (or “acute attacks”). Such precipitating events include gastrointestinal bleeding, infection (sepsis), portal vein thrombosis and dehydration. The onset of such an acute attack is likely to lead to hospitalization. The patient may suffer one of these acute attacks or a combination of these acute attacks.

A subject who has had or is suspected of having had an acute attack is treated according to the invention with L-ornithine phenyl acetate to prevent or reduce the likelihood of progression of the liver to the decompensated state. Consequently, L-ornithine phenyl acetate can prevent or reduce the likelihood of the medical consequences of liver decompensation such as hepatic encephalopathy. L-Ornithine phenyl acetate may be used to preserve liver function. Use of L-ornithine phenyl acetate may thus extend the life of a patient with liver disease. In one embodiment, the metabolic consequences of a gastrointestinal bleed such as hyperammonemia, hypoisoleucemia and reduced protein synthesis in the post-bleeding period are prevented.

Typically, treatment of subjects may begin as soon as possible after the onset or the suspected onset of a precipitating event (acute attack). Preferably, treatment of the subject begins prior to repeated acute attacks. More preferably, treatment of the subject begins following the first acute attack. Thus, in some embodiments, the subject treated with L-ornithine phenyl acetate is identified as having the onset or the suspected onset of a precipitating event (acute attack).

Treatment is typically given promptly after the start of an acute attack. Treatment may begin after the symptom(s) of an acute attack or suspected acute attack have been detected e.g. by a medic such as a physician, a paramedic or a nurse. Treatment may begin upon hospitalization of the subject. Treatment may thus begin within 6 hours, within 3 hours, within 2 hours or within 1 hour after the symptom(s) of an acute attack or suspected acute attack have been detected. Treatment of the subject may therefore begin from 1 to 48 hours, for example from 1 to 36 hours or from 1 to 24 hours after the symptom(s) of an acute attack or suspected acute attack have been detected.

Treatment may occur for up to 8 weeks, for example up to 6 weeks, up to 4 weeks or up to 2 weeks after the symptom(s) of an acute attack or suspected acute attack have been detected. Treatment may therefore occur for up to 48 hours, for example for up to 36 hours or for up to 24 hours after the symptom(s) of an acute attack or suspected acute attack have been detected. Typically, treatment occurs to the time when recovery from the acute precipitating event is evident.

L-Ornithine phenyl acetate may also be used to treat or ameliorate hyperammonemia. Thus, L-ornithine phenyl acetate may be administered to patients identified as having excess ammonia levels in the blood, or patients exhibiting symptoms of excess ammonia in the blood. L-Ornithine phenyl acetate may also be administered to reduce the risk of hyperammonemia. In some embodiments, L-ornithine phenyl acetate can be administered daily, for an indefinite period of time. For example, daily dosages may be administered for the life of the patient, or until a physician determines the patient no longer exhibits a risk for hyperammonemia. In some embodiments, a therapeutically effective amount of L-ornithine phenyl acetate is administered to reduce the risk of hyperammonemia. In some embodiments, a therapeutically effective amount of L-ornithine phenyl acetate is administered orally for the prophylaxis of hyperammonemia.

A therapeutically effective amount of L-ornithine phenyl acetate is administered to the subject. As will be readily apparent to one skilled in the art, the useful in vivo dosage to be administered and the particular mode of administration will vary depending upon the age, weight, the severity of the affliction, and mammalian species treated, the particular compounds employed, and the specific use for which these compounds are employed. (See e.g., Fingl et al. 1975, in “The Pharmacological Basis of Therapeutics”, which is hereby incorporated herein by reference in its entirety, with particular reference to Ch. 1, p. 1). The determination of effective dosage levels, that is the dosage levels necessary to achieve the desired result, can be accomplished by one skilled in the art using routine pharmacological methods. Typically, human clinical applications of products are commenced at lower dosage levels, with dosage level being increased until the desired effect is achieved. Alternatively, acceptable in vitro studies can be used to establish useful doses and routes of administration of the compositions identified by the present methods using established pharmacological methods.

A typical dose of L-ornithine phenyl acetate may be from about 0.02 to about 1.25 g/kg of bodyweight (preferably from about 0.1 to about 0.6 g/kg of bodyweight). A dosage may therefore be from about 500 mg to about 50 g (preferably about 5 g to about 40 g, and more preferably about 10 g to about 30 g).

A single daily dose may be administered. Alternatively, multiple doses, for example two, three, four or five doses may be administered. Such multiple doses may be administered over a period of one month or two weeks or one week. In some embodiments, a single dose or multiple doses such as two, three, four or five doses may be administered daily.

EXAMPLES AND EXPERIMENTAL METHODS

Additional embodiments are disclosed in further detail in the following examples, which are not in any way intended to limit the scope of the claims.

X-Ray Powder Diffraction (XRPD)

(RFD analysis was carried out on a Bruker D8 advance or Seimens D5000, scanning the samples between 4° and 50° 2θ. In embodiments using the Bruker D8 device, approximately 5 mg of a sample was gently compressed on the XRPD zero back ground single 96 well plate sample holder. The sample was then loaded into a Bruker D8-Discover diffractometer in transmission mode and analysed using the following experimental conditions.

Operator D8-Discover Raw Data Origin BRUKER-binary V3 (.RAW) Scan Axis Gonio Start Position [°2θ.] 4.0000 End Position [°2θ.] 49.9800 Step Size [°2θ.] 0.0200 Scan Step Time [s] 39.1393 Scan Type Continuous Offset [°2θ.] 0.0000 Divergence Slit Type Fixed Divergence Slit Size [°] 2.0000 Specimen Length [mm] 10.00 Receiving Slit Size [mm] 0.1000 Measurement Temperature 25.00 [° C.] Anode Material Cu K-Alpha1 [Å] 1.54060 K-Alpha2 [Å] 1.54443 K-Beta [Å] 1.39225 K-A2/K-A1 Ratio 0.50000 Generator Settings 40 mA, 40 kV Diffractometer Type Unknown Diffractometer Number 0 Goniometer Radius [mm] 250.00 Dist. Focus-Diverg. Slit [mm] 91.00 Incident Beam Monochromator No Spinning No

In embodiments using the Seimens D5000 device, approximately 5 mg of sample was gently compressed on glass slide containing a thin layer of holding grease. The sample was then loaded into a Seimens D5000 diffractometer running in reflection mode and analysed, whilst spinning, using the following experimental conditions.

Raw Data Origin Siemens-binary V2 (.RAW) Start Position [°2θ.] 3.0000 End Position [°2θ.] 50.000 Step Size [°2θ.] 0.0200 Scan Step Time [s] 0.8 Scan Type Continuous Offset [°2θ.] 0.0000 Divergence Slit Type Fixed Divergence Slit Size [°] 1.0000 Specimen Length [mm] various Receiving Slit Size [mm] 0.2000 Measurement Temperature [° C.] 20.00 Anode Material Cu K-Alpha1 [Å] 1.54060 K-Alpha2 [Å] 1.54443 K-Beta [Å] 1.39225 K-A2/K-A1 Ratio 0.50000 (nominal) Generator Settings 40 mA, 40 kV Diffractometer Type d5000 Diffractometer Number 0 Goniometer Radius [mm] 217.50 Incident Beam Monochromator No Diffracted Beam Monochromator (Graphite) Spinning Yes Single Crystal X-Ray Diffraction (SXRD)

All measurements were carried out using a Bruker Smart Apex diffractometer operating with Mo-Kα radiation. Unless otherwise specified the data were obtained in 60 ω-scan 10 s images collected in three separate settings of 2θ and φ.

Differential Scanning Calorimetry (DSC)

Approximately 5 mg of sample was weighed into an aluminium DSC pan and sealed with a pierced aluminium lid (non-hermetically). The sample pan was then loaded into a Seiko DSC6200 (equipped with a cooler), cooled, and held at 25° C. Once a stable heat-flow response was obtained, the sample and reference were then heated to about 250° C. at a scan rate of 10° C./min and the resulting heat flow response monitored. Prior to analysis, the instrument was temperature and heat-flow calibrated using an indium reference standard. Sample analysis was carried out by Muse measurement software where the temperatures of thermal events were quoted as the onset temperature, measured according to the manufacturer's specifications.

Thermogravimetric Gravimetric/Differential Thermal Analysis (TG/DTA)

Approximately 5 mg of sample was weighed into an aluminium pan and loaded into a simultaneous thermogravimetric/differential thermal analyser (DTA) and held at room temperature. The sample was then heated at a rate of 10° C./min from 25° C. to 300° C. during which time the change in sample weight was monitored along with any thermal events (DTA). Nitrogen was used as the purge gas, at a flow rate of 20 cm³/min. Prior to analysis the instrument was weight and temperature calibrated using a 100 mg reference weight and an indium reference standard, respectively.

Dynamic Vapor Sorption (DVS)

Approximately 10 mg of sample was placed into a wire-mesh vapor sorption balance pan and loaded into a DVS-1 dynamic vapor sorption balance supplied by Scientific and Medical Systems (SMS). The sample was then dried by maintaining a 0% humidity environment until no further weight change was recorded. The sample was then subjected to a ramping profile from 0-90% relative humidity (RH) at 10% increments, maintaining the sample at each step until a stable weight had been achieved (99.5% step completion). After completion of the sorption cycle, the sample was then dried using the same procedure. The weight change during the sorption/desorption cycles were then plotted, allowing for the hygroscopic nature of the sample to be determined.

¹H Nuclear Magnetic Resonance (NMR)

¹H NMR was performed on a Bruker AC200. An NMR of each sample was performed in d-H₂O and each sample was prepared to about 5 mg concentration. The NMR spectra for L-ornithine benzoate and L-ornithine phenyl acetate are provided in FIGS. 21 and 22, respectively.

Solubility Approximations

Approximately, 25 mg portions of the sample were placed in vials 5 volume increments of the appropriate solvent system were added. Between each addition, the mixture was checked for dissolution and if no dissolution was apparent, the mixture was warmed to 50° C., and checked again. The procedure was continued until dissolution was observed or when 100 volumes of solvent had been added.

HPLC Solubility Determinations

Slurries of each solvent were prepared and the samples shaken for about 48 hrs at 25° C. Each sample was then drawn through a filter, and the filtrate transferred to an HPLC vial for analysis. From the data the solubility of L-ornithine phenyl acetate for each solvent was determined.

Temperature Cycling Experiments

Using the information gathered from the solubility approximations, slurries of the sample were prepared in 24 selected solvent systems. The slurries were temperature cycled at 40° C. or 25° C. in 4 hour cycles for a period of 72 hours. The solids were visually checked for any obvious signs of degradation (i.e. color changes) and then, if not degraded, isolated by filtration. The solids were allowed to dry at ambient conditions for about 24 hours prior to analysis.

Crash Cooling Experiments

Crash cooling experiments were performed by placing saturated solutions of the sample, in the 24 selected solvent systems, in environments of 4° C. and −21° C. for about 48 hours. Any solid material was recovered and the solids were allowed to dry at ambient conditions for about 24 hours prior to analysis.

Evaporation Experiments

Evaporation experiments were conducted by allowing saturated solutions of the sample to evaporate freely at ambient conditions. The solid material was then recovered after the material had evaporated to dryness and analyzed.

Anti-Solvent Addition Experiments

Anti-solvent addition experiments were conducted by adding anti-solvent to saturated solutions of the sample. The addition was continued until there was no further precipitation and the samples adjusted to various temperature for 24 hours: elevated, ambient, 4° C. or −21°. The solid was then isolated and dried at ambient conditions for about 24 hours prior to analysis.

Polarized Light Microscopy (PLM)

The presence of crystallinity (birefringence) was determined using a Leica Leitz DMRB polarised optical microscope equipped with a high resolution Leica camera and image capture software (Firecam V.1.0). All images were recorded using a 10× objective, unless otherwise stated.

Silver Analysis

All silver analysis was carried out on an Agilent 7500ce ICP-MS.

Intrinsic Dissolution Rates

Approximately 100 mg of each form was compressed into discs by placing the material into a die (diameter 12 mm) and compressing the die under 5 tons of pressure in a hydraulic press for about 2 minutes. The dissolution instrument, Sotax AT7 conforms to EP2 and USP2 in which paddles were used to stir the media. Each form was tested under the following pH conditions; 1.0, 4.5 and 6.7, in the stationary disc mode (i.e. discs were added at time=0 seconds and allowed to sink to the bottom of the media). 1 cm³ aliquots of media were extracted from the dissolution pots at times 10, 20, 30, 40, 50, 60, 70, 80 and 120 seconds and tested for API concentration by HPLC. Dissolution curves were plotted and from the first 6 or 7 points on the curves the intrinsic dissolution rate curves were calculated. All tests were carried out at 37° C. and a paddle speed of 150 rpm.

HPLC-UV Instrument Details

Instrument: Agilent 1200

Column: Gemini C18, 5 μm, 150.0×4.6 mm

Column Temperature: 40° C.

Mobile Phase A: Phosphate Buffer

Mobile Phase B: Acetonitrile

Elution: Gradient

λ: 210 nm

Injection Volume: 10 μL

Flow Rate: 1 mL/min

Thin Layer Chromatography (TLC)

A small spot of solution containing the sample was applied to a plate, about one centimeter from the base. The plate is then dipped into the TLC tank (sealed container) containing methanol:ethyl acetate (95:5) solvent mixture. The solvent moves up the plate by capillary action and meets the sample mixture, which is dissolved and is carried up the plate by the solvent mixture. The number of spots was noted and the R_(f) values were calculated for each spot.

Infrared (IR)

Infrared spectroscopy was carried out on a Bruker ALPHA P spectrometer. Sufficient material was placed onto the centre of the plate of the spectrometer and the spectra were obtained using the following parameters:

-   -   Resolution: 4 cm−1     -   Background Scan Time: 16 scans     -   Sample Scan Time: 16 scans     -   Data Collection: 4000 to 400 cm−1     -   Result Spectrum: Transmittance     -   Software: OPUS version 6         Stabilities Studies: pH 1, 4, 7, 10 and 14 Environments

Slurries (supersaturated solution: about 250 μl of pH solution and solid was added until dissolution was no longer observed and ca. 100 mg of solid was in the slurry) were prepared for each form in a variety of pH environments; 1, 4, 7, 10 and 13.2. The slurries were shaken constantly for a period of 14 days and measurements taken at 7 and 14 day time points. Appropriate buffers were prepared for each pH and are detailed further below.

A buffer having a pH value of 1 was prepared by dissolving 372.75 mg of potassium chloride in 25 ml of deionized water to give a 0.2 M solution. Subsequently, 67 ml of 0.2 M hydrochloric acid was added (this was prepared from a 5 M solution; 10 ml was added to 40 ml of deionized water giving a 1 M solution which was diluted further; 20 ml was added to 80 ml of deionized water giving the required 0.2 M solution) to achieve the desired pH.

A buffer having a pH value of 4 was prepared by dissolving 1.02 g of potassium hydrogen phthalate in 50 ml of deionized water to give a 0.1 M solution.

A buffer having a pH value of 7 was prepared by dissolving 680.00 mg of potassium phosphate monobasic in 50 ml of deionized water to give a 0.1 M solution. Subsequently, 29.1 ml of 0.1 M sodium hydroxide was added (this was prepared from a 1 M solution; 5 ml was added to 45 ml of deionized water giving the required 0.1 M solution) to achieve the desired pH.

A buffer having a pH value of 10 was prepared by dissolving 210.00 mg of sodium bicarbonate in 50 ml of deionized water to give a 0.05 M solution. Subsequently, 10.7 ml of 0.1 M sodium hydroxide was added (this was prepared from a 1 M solution; 5 ml was added to 45 ml of deionized water giving the required 0.1 M solution) to achieve the desired pH.

A buffer having a pH value of pH 13.2 by dissolving 372.75 mg of potassium chloride in 25 ml of deionized water to give a 0.2 M solution. Subsequently, 66 ml of 0.2 M sodium hydroxide was added (this was prepared from a 1 M solution; 20 ml was added to 80 ml of deionized water giving the required 0.2 M solution) taking the pH to 13. 1M sodium hydroxide was then added drop wise to achieve the desired pH.

Example 1 Precipitating Crystalline Forms

Saturated solutions of L-ornithine phenyl acetate were subjected to temperature cycling, crash cooling, evaporation, or anti-solvent addition as described above. The precipitate was analyzed by PLM and XRPD to determine the crystalline form (if any). The results are summarized in TABLE 5.

Six unique crystalline forms were identified from the precipitation studies, Forms I-VI. However, Forms IV and VI were obtained from solutions of acetic acid, and NMR results confirmed these forms to be L-ornithine acetate. Meanwhile, Tests 540-611 utilized samples of L-ornithine phenyl acetate originally isolated by the addition of ethanol anti-solvent. Many of these example produced Form I, which is an ethanol solvate, and therefore it is believed these samples originally included residual ethanol. Consequently, Form I may not be reproduced for certain conditions if the original sample does not include residual ethanol.

TABLE 5 Examples of Preparing Crystalline Forms Crystallization Test Method Solvent Results 1 Temp. Cycling cyclohexanone Form II 2 Controlled Cool (4° C.) cyclohexanone No Solid 3 Controlled Cool (−21° C.) cyclohexanone Form V 4 Evaporation cyclohexanone Form V 5 Anti-Solvent (IPA) cyclohexanone No Solid Addition Elevated Temperature 6 Anti-Solvent (IPA) cyclohexanone Form II Addition Ambient Temperature 7 Anti-Solvent (IPA) cyclohexanone Form II Addition (4° C.) 8 Anti-Solvent (IPA) cyclohexanone Form II Addition (−21° C.) 9 Anti-Solvent (Ethanol) cyclohexanone Form II Addition Ambient Temperature 10 Anti-Solvent (Ethanol) cyclohexanone Form I Addition (4° C.) 11 Anti-Solvent (Ethanol) cyclohexanone Form I Addition (−21° C.) 12 Temp. Cycling ethanol/acetone Form II (50:50) 13 Controlled Cool (4° C.) ethanol/acetone No Solid (50:50) 14 Controlled Cool (−21° C.) ethanol/acetone Form III (50:50) 15 Evaporation ethanol/acetone Form II (50:50) 16 Anti-Solvent (IPA) ethanol/acetone Form II Addition Elevated (50:50) Temperature 17 Anti-Solvent (IPA) ethanol/acetone Form II Addition Ambient (50:50) Temperature 18 Anti-Solvent (IPA) ethanol/acetone Form II Addition (4° C.) (50:50) 19 Anti-Solvent (IPA) ethanol/acetone Form II Addition (−21° C.) (50:50) 20 Anti-Solvent (Ethanol) ethanol/acetone Form II Addition Ambient (50:50) Temperature 21 Anti-Solvent (Ethanol) ethanol/acetone Form I Addition (4° C.) (50:50) 22 Anti-Solvent (Ethanol) ethanol/acetone Form I Addition (−21° C.) (50:50) 23 Temp. Cycling acetic acid Form IV 24 Controlled Cool (4° C.) acetic acid No Solid 25 Controlled Cool (−21° C.) acetic acid No Solid 26 Evaporation acetic acid Form II 27 Anti-Solvent (IPA) acetic acid Form VI Addition Elevated Temperature 28 Anti-Solvent (IPA) acetic acid Form IV Addition Ambient Temperature 29 Anti-Solvent (IPA) acetic acid Form IV Addition (4° C.) 30 Anti-Solvent (IPA) acetic acid Form IV Addition (−21° C.) 31 Anti-Solvent (Ethanol) acetic acid Form IV Addition Ambient Temperature 32 Anti-Solvent (Ethanol) acetic acid Form IV Addition (4° C.) 33 Anti-Solvent (Ethanol) acetic acid Form IV Addition (−21° C.) 34 Temp. Cycling 1-propanol Form II 35 Controlled Cool (4° C.) 1-propanol Form II 36 Controlled Cool (−21° C.) 1-propanol Form II 37 Evaporation 1-propanol Form II 38 Anti-Solvent (IPA) 1-propanol Form II Addition Elevated Temperature 39 Anti-Solvent (IPA) 1-propanol Form II Addition Ambient Temperature 40 Anti-Solvent (IPA) 1-propanol Form II Addition (4° C.) 41 Anti-Solvent (IPA) 1-propanol Form II Addition (−21° C.) 42 Anti-Solvent (Ethanol) 1-propanol Form II Addition Ambient Temperature 43 Anti-Solvent (Ethanol) 1-propanol Form I/II Addition (4° C.) 44 Anti-Solvent (Ethanol) 1-propanol Form I Addition (−21° C.) 45 Temp. Cycling dimethylcarbonate Form II 46 Controlled Cool (4° C.) dimethylcarbonate No Solid 47 Controlled Cool (−21° C.) dimethylcarbonate Form II 48 Evaporation dimethylcarbonate Form II 49 Anti-Solvent (IPA) dimethylcarbonate Form II Addition Elevated Temperature 50 Anti-Solvent (IPA) dimethylcarbonate Form II Addition Ambient Temperature 51 Anti-Solvent (IPA) dimethylcarbonate Form II Addition (4° C.) 52 Anti-Solvent (IPA) dimethylcarbonate Form II Addition (−21° C.) 53 Anti-Solvent (Ethanol) dimethylcarbonate Form II Addition Ambient Temperature 54 Anti-Solvent (Ethanol) dimethylcarbonate Form I Addition (4° C.) 55 Anti-Solvent (Ethanol) dimethylcarbonate Form II Addition (−21° C.) 56 Temp. Cycling NMP Form II 57 Controlled Cool (4° C.) NMP Form II 58 Controlled Cool (−21° C.) NMP Form II 59 Evaporation NMP Form II 60 Anti-Solvent (IPA) NMP Form II Addition Elevated Temperature 61 Anti-Solvent (IPA) NMP Form II Addition Ambient Temperature 62 Anti-Solvent (IPA) NMP Form II Addition (4° C.) 63 Anti-Solvent (IPA) NMP Form II Addition (−21° C.) 64 Anti-Solvent (Ethanol) NMP Form II Addition Ambient Temperature 65 Anti-Solvent (Ethanol) NMP Form I/II Addition (4° C.) 66 Anti-Solvent (Ethanol) NMP Form II Addition (−21° C.) 67 Temp. Cycling EtOAc/cyclohexane Form II (1:2) 68 Controlled Cool (4° C.) EtOAc/cyclohexane No Solid (1:2) 69 Controlled Cool (−21° C.) EtOAc/cyclohexane No Solid (1:2) 70 Evaporation etOAc/cyclohexane Form II (1:2) 71 Anti-Solvent (IPA) etOAc/cyclohexane Form II Addition Elevated (1:2) Temperature 72 Anti-Solvent (IPA) etOAc/cyclohexane Form II Addition Ambient (1:2) Temperature 73 Anti-Solvent (IPA) etOAc/cyclohexane Form II Addition (4° C.) (1:2) 74 Anti-Solvent (IPA) etOAc/cyclohexane Form II Addition (−21° C.) (1:2) 75 Anti-Solvent (Ethanol) etOAc/cyclohexane Form II Addition Ambient (1:2) Temperature 76 Anti-Solvent (Ethanol) etOAc/cyclohexane Form I Addition (4° C.) (1:2) 77 Anti-Solvent (Ethanol) etOAc/cyclohexane Form I/II Addition (−21° C.) (1:2) 78 Temp. Cycling etOAc/toluene (1:2) Form II 79 Controlled Cool (4° C.) etOAc/toluene (1:2) No Solid 80 Controlled Cool (−21° C.) etOAc/toluene (1:2) Form II 81 Evaporation etOAc/toluene (1:2) Form II 82 Anti-Solvent (IPA) etOAc/toluene (1:2) Form II Addition Elevated Temperature 83 Anti-Solvent (IPA) etOAc/toluene (1:2) Form II Addition Ambient Temperature 84 Anti-Solvent (IPA) etOAc/toluene (1:2) Form II Addition (4° C.) 85 Anti-Solvent (IPA) etOAc/toluene (1:2) Form II Addition (−21° C.) 86 Anti-Solvent (Ethanol) etOAc/toluene (1:2) Form II Addition Ambient Temperature 87 Anti-Solvent (Ethanol) etOAc/toluene (1:2) Form I Addition (4° C.) 88 Anti-Solvent (Ethanol) etOAc/toluene (1:2) Form II Addition (−21° C.) 89 Temp. Cycling IPA/diisopropyl ether Form II (1:2) 90 Controlled Cool (4° C.) IPA/diisopropyl ether Form V (1:2) 91 Controlled Cool (−21° C.) IPA/diisopropyl ether Form II (1:2) 92 Evaporation IPA/diisopropyl ether Form II (1:2) 93 Anti-Solvent (IPA) IPA/diisopropyl ether Form II Addition Elevated (1:2) Temperature 94 Anti-Solvent (IPA) IPA/diisopropyl ether Form II Addition Ambient (1:2) Temperature 95 Anti-Solvent (IPA) IPA/diisopropyl ether Form II Addition (4° C.) (1:2) 96 Anti-Solvent (IPA) IPA/diisopropyl ether Form II Addition (−21° C.) (1:2) 97 Anti-Solvent (Ethanol) IPA/diisopropyl ether Form II Addition Ambient (1:2) Temperature 98 Anti-Solvent (Ethanol) IPA/diisopropyl ether Form I Addition (4° C.) (1:2) 99 Anti-Solvent (Ethanol) IPA/diisopropyl ether Form I/II Addition (−21° C.) (1:2) 100 Temp. Cycling DIPE Form II 101 Controlled Cool (4° C.) DIPE No Solid 102 Controlled Cool (−21° C.) DIPE Form V 103 Evaporation DIPE Form II 104 Anti-Solvent (IPA) DIPE Form II Addition Elevated Temperature 105 Anti-Solvent (IPA) DIPE Form II Addition Ambient Temperature 106 Anti-Solvent (IPA) DIPE Form II Addition (4° C.) 107 Anti-Solvent (IPA) DIPE Form II Addition (−21° C.) 108 Anti-Solvent (Ethanol) DIPE Form II Addition Ambient Temperature 109 Anti-Solvent (Ethanol) DIPE Form I Addition (4° C.) 110 Anti-Solvent (Ethanol) DIPE Form II Addition (−21° C.) 111 Temp. Cycling nitromethane/water No Solid (20%) 112 Controlled Cool (4° C.) nitromethane/water No Solid (20%) 113 Controlled Cool (−21° C.) nitromethane/water No Solid (20%) 114 Evaporation nitromethane/water Form II (20%) 115 Anti-Solvent (IPA) nitromethane/water No Solid Addition Elevated (20%) Temperature 116 Anti-Solvent (IPA) nitromethane/water Form II Addition Ambient (20%) Temperature 117 Anti-Solvent (IPA) nitromethane/water Form II Addition (4° C.) (20%) 118 Anti-Solvent (IPA) nitromethane/water Form II Addition (−21° C.) (20%) 119 Anti-Solvent (Ethanol) nitromethane/water Form II Addition Ambient (20%) Temperature 120 Anti-Solvent (Ethanol) nitromethane/water Form I Addition (4° C.) (20%) 121 Anti-Solvent (Ethanol) nitromethane/water Form I/II Addition (−21° C.) (20%) 122 Temp. Cycling acetone/water (20%) No Solid 123 Controlled Cool (4° C.) acetone/water (20%) Form II 124 Controlled Cool (−21° C.) acetone/water (20%) Form II 125 Evaporation acetone/water (20%) Form II 126 Anti-Solvent (IPA) acetone/water (20%) Form II Addition Elevated Temperature 127 Anti-Solvent (IPA) acetone/water (20%) Form II Addition Ambient Temperature 128 Anti-Solvent (IPA) acetone/water (20%) Form II Addition (4° C.) 129 Anti-Solvent (IPA) acetone/water (20%) Form II Addition (−21° C.) 130 Anti-Solvent (Ethanol) acetone/water (20%) Form II Addition Ambient Temperature 131 Anti-Solvent (Ethanol) acetone/water (20%) Form I Addition (4° C.) 132 Anti-Solvent (Ethanol) acetone/water (20%) Form II Addition (−21° C.) 133 Temp. Cycling 1,4 dioxane/water Form II (20%) 134 Controlled Cool (4° C.) 1,4 dioxane/water Form II (20%) 135 Controlled Cool (−21° C.) 1,4 dioxane/water No Solid (20%) 136 Evaporation 1,4 dioxane/water Form II (20%) 137 Anti-Solvent (IPA) 1,4 dioxane/water Form II Addition Elevated (20%) Temperature 138 Anti-Solvent (IPA) 1,4 dioxane/water Form II Addition Ambient (20%) Temperature 139 Anti-Solvent (IPA) 1,4 dioxane/water Form II Addition (4° C.) (20%) 140 Anti-Solvent (IPA) 1,4 dioxane/water Form II Addition (−21° C.) (20%) 141 Anti-Solvent (Ethanol) 1,4 dioxane/water Form II Addition Ambient (20%) Temperature 142 Anti-Solvent (Ethanol) 1,4 dioxane/water Form I Addition (4° C.) (20%) 143 Anti-Solvent (Ethanol) 1,4 dioxane/water Form II Addition (−21° C.) (20%) 144 Temp. Cycling diethyl ether Form II 145 Controlled Cool (4° C.) diethyl ether No Solid 146 Controlled Cool (−21° C.) diethyl ether No Solid 147 Evaporation diethyl ether Form II 148 Anti-Solvent (IPA) diethyl ether Form II Addition Elevated Temperature 149 Anti-Solvent (IPA) diethyl ether Form II Addition Ambient Temperature 150 Anti-Solvent (IPA) diethyl ether Form II Addition (4° C.) 151 Anti-Solvent (IPA) diethyl ether Form II Addition (−21° C.) 152 Anti-Solvent (Ethanol) diethyl ether Form II Addition Ambient Temperature 153 Anti-Solvent (Ethanol) diethyl ether Form I Addition (4° C.) 154 Anti-Solvent (Ethanol) diethyl ether Form I/II Addition (−21° C.) 155 Temp. Cycling ethylene glycol Form II 156 Controlled Cool (4° C.) ethylene glycol No Solid 157 Controlled Cool (−21° C.) ethylene glycol No Solid 158 Evaporation ethylene glycol No Solid 159 Anti-Solvent (IPA) ethylene glycol Form II Addition Elevated Temperature 160 Anti-Solvent (IPA) ethylene glycol Form II Addition Ambient Temperature 161 Anti-Solvent (IPA) ethylene glycol Form II Addition (4° C.) 162 Anti-Solvent (IPA) ethylene glycol Form II Addition (−21° C.) 163 Anti-Solvent (Ethanol) ethylene glycol Form II Addition Ambient Temperature 164 Anti-Solvent (Ethanol) ethylene glycol Form II Addition (4° C.) 165 Anti-Solvent (Ethanol) ethylene glycol Form II Addition (−21° C.) 166 Temp. Cycling meOAc/water (20%) No Solid 167 Controlled Cool (4° C.) meOAc/water (20%) No Solid 168 Controlled Cool (−21° C.) meOAc/water (20%) No Solid 169 Evaporation meOAc/water (20%) Form II 170 Anti-Solvent (IPA) meOAc/water (20%) Form II Addition Elevated Temperature 171 Anti-Solvent (IPA) meOAc/water (20%) Form II Addition Ambient Temperature 172 Anti-Solvent (IPA) meOAc/water (20%) Form II Addition (4° C.) 173 Anti-Solvent (IPA) meOAc/water (20%) Form II Addition (−21° C.) 174 Anti-Solvent (Ethanol) meOAc/water (20%) Form II Addition Ambient Temperature 175 Anti-Solvent (Ethanol) meOAc/water (20%) Form I/II Addition (4° C.) 176 Anti-Solvent (Ethanol) meOAc/water (20%) Form II Addition (−21° C.) 177 Temp. Cycling meOH/acetone Form II (50:50) 178 Controlled Cool (4° C.) meOH/acetone No Solid (50:50) 179 Controlled Cool (−21° C.) meOH/acetone No Solid (50:50) 180 Evaporation meOH/acetone Form II (50:50) 181 Anti-Solvent (IPA) meOH/acetone Form II Addition Elevated (50:50) Temperature 182 Anti-Solvent (IPA) meOH/acetone Form II Addition Ambient (50:50) Temperature 183 Anti-Solvent (IPA) meOH/acetone Form II Addition (4° C.) (50:50) 184 Anti-Solvent (IPA) meOH/acetone Form II Addition (−21° C.) (50:50) 185 Anti-Solvent (Ethanol) meOH/acetone Form II Addition Ambient (50:50) Temperature 186 Anti-Solvent (Ethanol) meOH/acetone Form I Addition (4° C.) (50:50) 187 Anti-Solvent (Ethanol) meOH/acetone Form I/II Addition (−21° C.) (50:50) 188 Temp. Cycling DMF Form II 189 Controlled Cool (4° C.) DMF Form II 190 Controlled Cool (−21° C.) DMF Form II 191 Evaporation DMF Form II 192 Anti-Solvent (IPA) DMF Form II Addition Elevated Temperature 193 Anti-Solvent (IPA) DMF Form II Addition Ambient Temperature 194 Anti-Solvent (IPA) DMF Form II Addition (4° C.) 195 Anti-Solvent (IPA) DMF Form II Addition (−21° C.) 196 Anti-Solvent (Ethanol) DMF Form II Addition Ambient Temperature 197 Anti-Solvent (Ethanol) DMF Form I/II Addition (4° C.) 198 Anti-Solvent (Ethanol) DMF Form II Addition (−21° C.) 199 Temp. Cycling 2-butanol Form II 200 Controlled Cool (4° C.) 2-butanol No Solid 201 Controlled Cool (−21° C.) 2-butanol No Solid 202 Evaporation 2-butanol Form II 203 Anti-Solvent (IPA) 2-butanol Form III Addition Elevated Temperature 204 Anti-Solvent (IPA) 2-butanol Form II Addition Ambient Temperature 205 Anti-Solvent (IPA) 2-butanol Form II Addition (4° C.) 206 Anti-Solvent (IPA) 2-butanol Form II Addition (−21° C.) 207 Anti-Solvent (Ethanol) 2-butanol Form II Addition Ambient Temperature 208 Anti-Solvent (Ethanol) 2-butanol Form I/II Addition (4° C.) 209 Anti-Solvent (Ethanol) 2-butanol Form I/II Addition (−21° C.) 210 Temp. Cycling cumene Form II 211 Controlled Cool (4° C.) cumene No Solid 212 Controlled Cool (−21° C.) cumene No Solid 213 Evaporation cumene Form II 214 Anti-Solvent (IPA) cumene Form II Addition Elevated Temperature 215 Anti-Solvent (IPA) cumene Form II Addition Ambient Temperature 216 Anti-Solvent (IPA) cumene Form II Addition (4° C.) 217 Anti-Solvent (IPA) cumene Form II Addition (−21° C.) 218 Anti-Solvent (Ethanol) cumene Form II Addition Ambient Temperature 219 Anti-Solvent (Ethanol) cumene Form II Addition (4° C.) 220 Anti-Solvent (Ethanol) cumene Form I/II Addition (−21° C.) 221 Temp. Cycling ethyl formate Form II 222 Controlled Cool (4° C.) ethyl formate No Solid 223 Controlled Cool (−21° C.) ethyl formate Form II 224 Evaporation ethyl formate Form II 225 Anti-Solvent (IPA) ethyl formate Form II Addition Elevated Temperature 226 Anti-Solvent (IPA) ethyl formate Form II Addition Ambient Temperature 227 Anti-Solvent (IPA) ethyl formate Form II Addition (4° C.) 228 Anti-Solvent (IPA) ethyl formate Form II Addition (−21° C.) 229 Anti-Solvent (Ethanol) ethyl formate Form II Addition Ambient Temperature 230 Anti-Solvent (Ethanol) ethyl formate Form I Addition (4° C.) 231 Anti-Solvent (Ethanol) ethyl formate Form I/II Addition (−21° C.) 232 Temp. Cycling isobutyl acetate Form II 233 Controlled Cool (4° C.) isobutyl acetate No Solid 234 Controlled Cool (−21° C.) isobutyl acetate Form II 235 Evaporation isobutyl acetate No Solid 236 Anti-Solvent (IPA) isobutyl acetate Form II Addition Elevated Temperature 237 Anti-Solvent (IPA) isobutyl acetate Form II Addition Ambient Temperature 238 Anti-Solvent (IPA) isobutyl acetate Form II Addition (4° C.) 239 Anti-Solvent (IPA) isobutyl acetate Form III Addition (−21° C.) 240 Anti-Solvent (Ethanol) isobutyl acetate Form II Addition Ambient Temperature 241 Anti-Solvent (Ethanol) isobutyl acetate Form II Addition (4° C.) 242 Anti-Solvent (Ethanol) isobutyl acetate Form I/II Addition (−21° C.) 243 Temp. Cycling 3-methyl-1-butanol Form II 244 Controlled Cool (4° C.) 3-methyl-1-butanol No Solid 245 Controlled Cool (−21° C.) 3-methyl-1-butanol No Solid 246 Evaporation 3-methyl-1-butanol Form II 247 Anti-Solvent (IPA) 3-methyl-1-butanol Form II Addition Elevated Temperature 248 Anti-Solvent (IPA) 3-methyl-1-butanol Form II Addition Ambient Temperature 249 Anti-Solvent (IPA) 3-methyl-1-butanol Form II Addition (4° C.) 250 Anti-Solvent (IPA) 3-methyl-1-butanol Form II Addition (−21° C.) 251 Anti-Solvent (Ethanol) 3-methyl-1-butanol Form II Addition Ambient Temperature 252 Anti-Solvent (Ethanol) 3-methyl-1-butanol Form I/II Addition (4° C.) 253 Anti-Solvent (Ethanol) 3-methyl-1-butanol Form I/II Addition (−21° C.) 254 Temp. Cycling anisole Form II 255 Controlled Cool (4° C.) anisole No Solid 256 Controlled Cool (−21° C.) anisole Form II 257 Evaporation anisole Form II 258 Anti-Solvent (IPA) anisole Form II Addition Elevated Temperature 259 Anti-Solvent (IPA) anisole Form II Addition Ambient Temperature 260 Anti-Solvent (IPA) anisole Form II Addition (4° C.) 261 Anti-Solvent (IPA) anisole Form II/IV Addition (−21° C.) 262 Anti-Solvent (Ethanol) anisole Form II Addition Ambient Temperature 263 Anti-Solvent (Ethanol) anisole Form II Addition (4° C.) 264 Anti-Solvent (Ethanol) anisole Form I Addition (−21° C.) 265 Temp. Cycling IPA/isopropyl acetate Form II (1:2) 266 Controlled Cool (4° C.) IPA/isopropyl acetate No Solid (1:2) 267 Controlled Cool (−21° C.) IPA/isopropyl acetate No Solid (1:2) 268 Evaporation IPA/isopropyl acetate Form II (1:2) 269 Anti-Solvent (IPA) IPA/isopropyl acetate Form II Addition Elevated (1:2) Temperature 270 Anti-Solvent (IPA) IPA/isopropyl acetate Form II Addition Ambient (1:2) Temperature 271 Anti-Solvent (IPA) IPA/isopropyl acetate Form II Addition (4° C.) (1:2) 272 Anti-Solvent (IPA) IPA/isopropyl acetate Form II Addition (−21° C.) (1:2) 273 Anti-Solvent (Ethanol) IPA/isopropyl acetate Form II Addition Ambient (1:2) Temperature 274 Anti-Solvent (Ethanol) IPA/isopropyl acetate Form II Addition (4° C.) (1:2) 275 Anti-Solvent (Ethanol) IPA/isopropyl acetate Form I Addition (−21° C.) (1:2) 276 Temp. Cycling EtOH: 1% H₂0 Form II 277 Controlled Cool (4° C.) EtOH: 1% H₂0 No Solid 278 Controlled Cool (−21° C.) EtOH: 1% H₂0 No Solid 279 Evaporation EtOH: 1% H₂0 No Solid 280 Anti-Solvent (IPA) EtOH: 1% H₂0 No Solid Addition Elevated Temperature 281 Anti-Solvent (IPA) EtOH: 1% H₂0 No Solid Addition Ambient Temperature 282 Anti-Solvent (IPA) EtOH: 1% H₂0 No Solid Addition (4° C.) 283 Anti-Solvent (IPA) EtOH: 1% H₂0 No Solid Addition (−21° C.) 284 Anti-Solvent (Ethanol) EtOH: 1% H₂0 No Solid Addition Ambient Temperature 285 Anti-Solvent (Ethanol) EtOH: 1% H₂0 No Solid Addition (4° C.) 286 Anti-Solvent (Ethanol) EtOH: 1% H₂0 No Solid Addition (−21° C.) 287 Temp. Cycling EtOH: 3% H₂0 Form II 288 Controlled Cool (4° C.) EtOH: 3% H₂0 No Solid 289 Controlled Cool (−21° C.) EtOH: 3% H₂0 No Solid 290 Evaporation EtOH: 3% H₂0 No Solid 291 Anti-Solvent (IPA) EtOH: 3% H₂0 No Solid Addition Elevated Temperature 292 Anti-Solvent (IPA) EtOH: 3% H₂0 No Solid Addition Ambient Temperature 293 Anti-Solvent (IPA) EtOH: 3% H₂0 No Solid Addition (4° C.) 294 Anti-Solvent (IPA) EtOH: 3% H₂0 No Solid Addition (−21° C.) 295 Anti-Solvent (Ethanol) EtOH: 3% H₂0 No Solid Addition Ambient Temperature 296 Anti-Solvent (Ethanol) EtOH: 3% H₂0 No Solid Addition (4° C.) 297 Anti-Solvent (Ethanol) EtOH: 3% H₂0 No Solid Addition (−21° C.) 298 Temp. Cycling EtOH: 5% H₂0 Form II 299 Controlled Cool (4° C.) EtOH: 5% H₂0 No Solid 300 Controlled Cool (−21° C.) EtOH: 5% H₂0 No Solid 301 Evaporation EtOH: 5% H₂0 Form II 302 Anti-Solvent (IPA) EtOH: 5% H₂0 No Solid Addition Elevated Temperature 303 Anti-Solvent (IPA) EtOH: 5% H₂0 Form II Addition Ambient Temperature 304 Anti-Solvent (IPA) EtOH: 5% H₂0 No Solid Addition (4° C.) 305 Anti-Solvent (IPA) EtOH: 5% H₂0 No Solid Addition (−21° C.) 306 Anti-Solvent (Ethanol) EtOH: 5% H₂0 No Solid Addition Ambient Temperature 307 Anti-Solvent (Ethanol) EtOH: 5% H₂0 No Solid Addition (4° C.) 308 Anti-Solvent (Ethanol) EtOH: 5% H₂0 No Solid Addition (−21° C.) 309 Temp. Cycling IPA: 1% H₂0 Form II 310 Controlled Cool (4° C.) IPA: 1% H₂0 No Solid 311 Controlled Cool (−21° C.) IPA: 1% H₂0 No Solid 312 Evaporation IPA: 1% H₂0 No Solid 313 Anti-Solvent (IPA) IPA: 1% H₂0 No Solid Addition Elevated Temperature 314 Anti-Solvent (IPA) IPA: 1% H₂0 No Solid Addition Ambient Temperature 315 Anti-Solvent (IPA) IPA: 1% H₂0 No Solid Addition (4° C.) 316 Anti-Solvent (IPA) IPA: 1% H₂0 No Solid Addition (−21° C.) 317 Anti-Solvent (Ethanol) IPA: 1% H₂0 No Solid Addition Ambient Temperature 318 Anti-Solvent (Ethanol) IPA: 1% H₂0 No Solid Addition (4° C.) 319 Anti-Solvent (Ethanol) IPA: 1% H₂0 No Solid Addition (−21° C.) 320 Temp. Cycling IPA: 3% H₂0 Form II 321 Controlled Cool (4° C.) IPA: 3% H₂0 No Solid 322 Controlled Cool (−21° C.) IPA: 3% H₂0 No Solid 323 Evaporation IPA: 3% H₂0 No Solid 324 Anti-Solvent (IPA) IPA: 3% H₂0 No Solid Addition Elevated Temperature 325 Anti-Solvent (IPA) IPA: 3% H₂0 No Solid Addition Ambient Temperature 326 Anti-Solvent (IPA) IPA: 3% H₂0 No Solid Addition (4° C.) 327 Anti-Solvent (IPA) IPA: 3% H₂0 No Solid Addition (−21° C.) 328 Anti-Solvent (Ethanol) IPA: 3% H₂0 No Solid Addition Ambient Temperature 329 Anti-Solvent (Ethanol) IPA: 3% H₂0 No Solid Addition (4° C.) 330 Anti-Solvent (Ethanol) IPA: 3% H₂0 No Solid Addition (−21° C.) 331 Temp. Cycling IPA: 5% H₂0 Form II 332 Controlled Cool (4° C.) IPA: 5% H₂0 No Solid 333 Controlled Cool (−21° C.) IPA: 5% H₂0 No Solid 334 Evaporation IPA: 5% H₂0 Form II 335 Anti-Solvent (IPA) IPA: 5% H₂0 No Solid Addition Elevated Temperature 336 Anti-Solvent (IPA) IPA: 5% H₂0 No Solid Addition Ambient Temperature 337 Anti-Solvent (IPA) IPA: 5% H₂0 No Solid Addition (4° C.) 338 Anti-Solvent (IPA) IPA: 5% H₂0 No Solid Addition (−21° C.) 339 Anti-Solvent (Ethanol) IPA: 5% H₂0 No Solid Addition Ambient Temperature 340 Anti-Solvent (Ethanol) IPA: 5% H₂0 No Solid Addition (4° C.) 341 Anti-Solvent (Ethanol) IPA: 5% H₂0 No Solid Addition (−21° C.) 342 Temp. Cycling ACN: 1% H₂0 Form II 343 Controlled Cool (4° C.) ACN: 1% H₂0 No Solid 344 Controlled Cool (−21° C.) ACN: 1% H₂0 No Solid 345 Evaporation ACN: 1% H₂0 Form II 346 Anti-Solvent (IPA) ACN: 1% H₂0 No Solid Addition Elevated Temperature 347 Anti-Solvent (IPA) ACN: 1% H₂0 No Solid Addition Ambient Temperature 348 Anti-Solvent (IPA) ACN: 1% H₂0 No Solid Addition (4° C.) 349 Anti-Solvent (IPA) ACN: 1% H₂0 No Solid Addition (−21° C.) 350 Anti-Solvent (Ethanol) ACN: 1% H₂0 No Solid Addition Ambient Temperature 351 Anti-Solvent (Ethanol) ACN: 1% H₂0 No Solid Addition (4° C.) 352 Anti-Solvent (Ethanol) ACN: 1% H₂0 No Solid Addition (−21° C.) 353 Temp. Cycling ACN: 6% H₂0 Form II 354 Controlled Cool (4° C.) ACN: 6% H₂0 No Solid 355 Controlled Cool (−21° C.) ACN: 6% H₂0 No Solid 356 Evaporation ACN: 6% H₂0 Form II 357 Anti-Solvent (IPA) ACN: 6% H₂0 No Solid Addition Elevated Temperature 358 Anti-Solvent (IPA) ACN: 6% H₂0 No Solid Addition Ambient Temperature 359 Anti-Solvent (IPA) ACN: 6% H₂0 No Solid Addition (4° C.) 360 Anti-Solvent (IPA) ACN: 6% H₂0 No Solid Addition (−21° C.) 361 Anti-Solvent (Ethanol) ACN: 6% H₂0 No Solid Addition Ambient Temperature 362 Anti-Solvent (Ethanol) ACN: 6% H₂0 No Solid Addition (4° C.) 363 Anti-Solvent (Ethanol) ACN: 6% H₂0 No Solid Addition (−21° C.) 364 Temp. Cycling ACN: 12% H₂0 No Solid 365 Controlled Cool (4° C.) ACN: 12% H₂0 No Solid 366 Controlled Cool (−21° C.) ACN: 12% H₂0 No Solid 367 Evaporation ACN: 12% H₂0 Form II 368 Anti-Solvent (IPA) ACN: 12% H₂0 No Solid Addition Elevated Temperature 369 Anti-Solvent (IPA) ACN: 12% H₂0 Form II Addition Ambient Temperature 370 Anti-Solvent (IPA) ACN: 12% H₂0 No Solid Addition (4° C.) 371 Anti-Solvent (IPA) ACN: 12% H₂0 Form II Addition (−21° C.) 372 Anti-Solvent (Ethanol) ACN: 12% H₂0 No Solid Addition Ambient Temperature 373 Anti-Solvent (Ethanol) ACN: 12% H₂0 No Solid Addition (4° C.) 374 Anti-Solvent (Ethanol) ACN: 12% H₂0 No Solid Addition (−21° C.) 375 Temp. Cycling DMF: 5% H₂0 Form II 376 Controlled Cool (4° C.) DMF: 5% H₂0 No Solid 377 Controlled Cool (−21° C.) DMF: 5% H₂0 No Solid 378 Evaporation DMF: 5% H₂0 No Solid 379 Anti-Solvent (IPA) DMF: 5% H₂0 No Solid Addition Elevated Temperature 380 Anti-Solvent (IPA) DMF: 5% H₂0 No Solid Addition Ambient Temperature 381 Anti-Solvent (IPA) DMF: 5% H₂0 No Solid Addition (4° C.) 382 Anti-Solvent (IPA) DMF: 5% H₂0 No Solid Addition (−21° C.) 383 Anti-Solvent (Ethanol) DMF: 5% H₂0 No Solid Addition Ambient Temperature 384 Anti-Solvent (Ethanol) DMF: 5% H₂0 No Solid Addition (4° C.) 385 Anti-Solvent (Ethanol) DMF: 5% H₂0 No Solid Addition (−21° C.) 386 Temp. Cycling DMF: 15% H₂0 Form II 387 Controlled Cool (4° C.) DMF: 15% H₂0 No Solid 388 Controlled Cool (−21° C.) DMF: 15% H₂0 No Solid 389 Evaporation DMF: 15% H₂0 No Solid 390 Anti-Solvent (IPA) DMF: 15% H₂0 No Solid Addition Elevated Temperature 391 Anti-Solvent (IPA) DMF: 15% H₂0 No Solid Addition Ambient Temperature 392 Anti-Solvent (IPA) DMF: 15% H₂0 No Solid Addition (4° C.) 393 Anti-Solvent (IPA) DMF: 15% H₂0 No Solid Addition (−21° C.) 394 Anti-Solvent (Ethanol) DMF: 15% H₂0 No Solid Addition Ambient Temperature 395 Anti-Solvent (Ethanol) DMF: 15% H₂0 No Solid Addition (4° C.) 396 Anti-Solvent (Ethanol) DMF: 15% H₂0 No Solid Addition (−21° C.) 397 Temp. Cycling DMF: 30% H₂0 Form II 398 Controlled Cool (4° C.) DMF: 30% H₂0 Form II 399 Controlled Cool (−21° C.) DMF: 30% H₂0 Form II 400 Evaporation DMF: 30% H₂0 Form II 401 Anti-Solvent (IPA) DMF: 30% H₂0 Form II Addition Elevated Temperature 402 Anti-Solvent (IPA) DMF: 30% H₂0 Form II Addition Ambient Temperature 403 Anti-Solvent (IPA) DMF: 30% H₂0 Form II Addition (4° C.) 404 Anti-Solvent (IPA) DMF: 30% H₂0 Form II Addition (−21° C.) 405 Anti-Solvent (Ethanol) DMF: 30% H₂0 Form II Addition Ambient Temperature 406 Anti-Solvent (Ethanol) DMF: 30% H₂0 No Solid Addition (4° C.) 407 Anti-Solvent (Ethanol) DMF: 30% H₂0 Form II Addition (−21° C.) 408 Temp. Cycling 1,4-dioxane: 1% H₂0 Form II 409 Controlled Cool (4° C.) 1,4-dioxane: 1% H₂0 No Solid 410 Controlled Cool (−21° C.) 1,4-dioxane: 1% H₂0 No Solid 411 Evaporation 1,4-dioxane: 1% H₂0 No Solid 412 Anti-Solvent (IPA) 1,4-dioxane: 1% H₂0 No Solid Addition Elevated Temperature 413 Anti-Solvent (IPA) 1,4-dioxane: 1% H₂0 No Solid Addition Ambient Temperature 414 Anti-Solvent (IPA) 1,4-dioxane: 1% H₂0 No Solid Addition (4° C.) 415 Anti-Solvent (IPA) 1,4-dioxane: 1% H₂0 No Solid Addition (−21° C.) 416 Anti-Solvent (Ethanol) 1,4-dioxane: 1% H₂0 No Solid Addition Ambient Temperature 417 Anti-Solvent (Ethanol) 1,4-dioxane: 1% H₂0 No Solid Addition (4° C.) 418 Anti-Solvent (Ethanol) 1,4-dioxane: 1% H₂0 No Solid Addition (−21° C.) 419 Temp. Cycling 1,4-dioxane: 3% H₂0 Form II 420 Controlled Cool (4° C.) 1,4-dioxane: 3% H₂0 No Solid 421 Controlled Cool (−21° C.) 1,4-dioxane: 3% H₂0 No Solid 422 Evaporation 1,4-dioxane: 3% H₂0 Form II 423 Anti-Solvent (IPA) 1,4-dioxane: 3% H₂0 No Solid Addition Elevated Temperature 424 Anti-Solvent (IPA) 1,4-dioxane: 3% H₂0 No Solid Addition Ambient Temperature 425 Anti-Solvent (IPA) 1,4-dioxane: 3% H₂0 No Solid Addition (4° C.) 426 Anti-Solvent (IPA) 1,4-dioxane: 3% H₂0 No Solid Addition (−21° C.) 427 Anti-Solvent (Ethanol) 1,4-dioxane: 3% H₂0 No Solid Addition Ambient Temperature 428 Anti-Solvent (Ethanol) 1,4-dioxane: 3% H₂0 No Solid Addition (4° C.) 429 Anti-Solvent (Ethanol) 1,4-dioxane: 3% H₂0 No Solid Addition (−21° C.) 430 Temp. Cycling 1,4-dioxane: 10% H₂0 Form II 431 Controlled Cool (4° C.) 1,4-dioxane: 10% H₂0 No Solid 432 Controlled Cool (−21° C.) 1,4-dioxane: 10% H₂0 No Solid 433 Evaporation 1,4-dioxane: 10% H₂0 Form II 434 Anti-Solvent (IPA) 1,4-dioxane: 10% H₂0 No Solid Addition Elevated Temperature 435 Anti-Solvent (IPA) 1,4-dioxane: 10% H₂0 No Solid Addition Ambient Temperature 436 Anti-Solvent (IPA) 1,4-dioxane: 10% H₂0 No Solid Addition (4° C.) 437 Anti-Solvent (IPA) 1,4-dioxane: 10% H₂0 No Solid Addition (−21° C.) 438 Anti-Solvent (Ethanol) 1,4-dioxane: 10% H₂0 No Solid Addition Ambient Temperature 439 Anti-Solvent (Ethanol) 1,4-dioxane: 10% H₂0 No Solid Addition (4° C.) 440 Anti-Solvent (Ethanol) 1,4-dioxane: 10% H₂0 No Solid Addition (−21° C.) 441 Temp. Cycling MeOH: 5% H₂0 Form II 442 Controlled Cool (4° C.) MeOH: 5% H₂0 No Solid 443 Controlled Cool (−21° C.) MeOH: 5% H₂0 No Solid 444 Evaporation MeOH: 5% H₂0 Form II 445 Anti-Solvent (IPA) MeOH: 5% H₂0 Form II Addition Elevated Temperature 446 Anti-Solvent (IPA) MeOH: 5% H₂0 Form II Addition Ambient Temperature 447 Anti-Solvent (IPA) MeOH: 5% H₂0 Form II Addition (4° C.) 448 Anti-Solvent (IPA) MeOH: 5% H₂0 Form II Addition (−21° C.) 449 Anti-Solvent (Ethanol) MeOH: 5% H₂0 No Solid Addition Ambient Temperature 450 Anti-Solvent (Ethanol) MeOH: 5% H₂0 Form II Addition (4° C.) 451 Anti-Solvent (Ethanol) MeOH: 5% H₂0 Form II Addition (−21° C.) 452 Temp. Cycling MeOH: 20% H₂0 No Solid 453 Controlled Cool (4° C.) MeOH: 20% H₂0 Form II 454 Controlled Cool (−21° C.) MeOH: 20% H₂0 Form II 455 Evaporation MeOH: 20% H₂0 Form II 456 Anti-Solvent (IPA) MeOH: 20% H₂0 Form II Addition Elevated Temperature 457 Anti-Solvent (IPA) MeOH: 20% H₂0 Form II Addition Ambient Temperature 458 Anti-Solvent (IPA) MeOH: 20% H₂0 Form II Addition (4° C.) 459 Anti-Solvent (IPA) MeOH: 20% H₂0 Form II Addition (−21° C.) 460 Anti-Solvent (Ethanol) MeOH: 20% H₂0 Form II Addition Ambient Temperature 461 Anti-Solvent (Ethanol) MeOH: 20% H₂0 Form II Addition (4° C.) 462 Anti-Solvent (Ethanol) MeOH: 20% H₂0 Form I/II Addition (−21° C.) 463 Temp. Cycling MeOH: 50% H₂0 Form II 464 Controlled Cool (4° C.) MeOH: 50% H₂0 Form II 465 Controlled Cool (−21° C.) MeOH: 50% H₂0 Form II 466 Evaporation MeOH: 50% H₂0 No Solid 467 Anti-Solvent (IPA) MeOH: 50% H₂0 Form II Addition Elevated Temperature 468 Anti-Solvent (IPA) MeOH: 50% H₂0 No Solid Addition Ambient Temperature 469 Anti-Solvent (IPA) MeOH: 50% H₂0 Form II Addition (4° C.) 470 Anti-Solvent (IPA) MeOH: 50% H₂0 No Solid Addition (−21° C.) 471 Anti-Solvent (Ethanol) MeOH: 50% H₂0 Form II Addition Ambient Temperature 472 Anti-Solvent (Ethanol) MeOH: 50% H₂0 Form I Addition (4° C.) 473 Anti-Solvent (Ethanol) MeOH: 50% H₂0 Form I/II Addition (−21° C.) 474 Temp. Cycling THF: 1% H₂0 Form II 475 Controlled Cool (4° C.) THF: 1% H₂0 No Solid 476 Controlled Cool (−21° C.) THF: 1% H₂0 No Solid 477 Evaporation THF: 1% H₂0 Form II 478 Anti-Solvent (IPA) THF: 1% H₂0 No Solid Addition Elevated Temperature 479 Anti-Solvent (IPA) THF: 1% H₂0 No Solid Addition Ambient Temperature 480 Anti-Solvent (IPA) THF: 1% H₂0 No Solid Addition (4° C.) 481 Anti-Solvent (IPA) THF: 1% H₂0 No Solid Addition (−21° C.) 482 Anti-Solvent (Ethanol) THF: 1% H₂0 No Solid Addition Ambient Temperature 483 Anti-Solvent (Ethanol) THF: 1% H₂0 No Solid Addition (4° C.) 484 Anti-Solvent (Ethanol) THF: 1% H₂0 No Solid Addition (−21° C.) 485 Temp. Cycling THF: 3% H₂0 Form II 486 Controlled Cool (4° C.) THF: 3% H₂0 No Solid 487 Controlled Cool (−21° C.) THF: 3% H₂0 No Solid 488 Evaporation THF: 3% H₂0 No Solid 489 Anti-Solvent (IPA) THF: 3% H₂0 No Solid Addition Elevated Temperature 490 Anti-Solvent (IPA) THF: 3% H₂0 Form II Addition Ambient Temperature 491 Anti-Solvent (IPA) THF: 3% H₂0 No Solid Addition (4° C.) 492 Anti-Solvent (IPA) THF: 3% H₂0 No Solid Addition (−21° C.) 493 Anti-Solvent (Ethanol) THF: 3% H₂0 No Solid Addition Ambient Temperature 494 Anti-Solvent (Ethanol) THF: 3% H₂0 No Solid Addition (4° C.) 495 Anti-Solvent (Ethanol) THF: 3% H₂0 No Solid Addition (−21° C.) 496 Temp. Cycling THF: 5% H₂0 No Solid 497 Controlled Cool (4° C.) THF: 5% H₂0 No Solid 498 Controlled Cool (−21° C.) THF: 5% H₂0 No Solid 499 Evaporation THF: 5% H₂0 Form II 500 Anti-Solvent (IPA) THF: 5% H₂0 No Solid Addition Elevated Temperature 501 Anti-Solvent (IPA) THF: 5% H₂0 No Solid Addition Ambient Temperature 502 Anti-Solvent (IPA) THF: 5% H₂0 Form II Addition (4° C.) 503 Anti-Solvent (IPA) THF: 5% H₂0 No Solid Addition (−21° C.) 504 Anti-Solvent (Ethanol) THF: 5% H₂0 No Solid Addition Ambient Temperature 505 Anti-Solvent (Ethanol) THF: 5% H₂0 No Solid Addition (4° C.) 506 Anti-Solvent (Ethanol) THF: 5% H₂0 No Solid Addition (−21° C.) 507 Temp. Cycling butan-1-ol: 1% H₂0 Form II 508 Controlled Cool (4° C.) butan-1-ol: 1% H₂0 No Solid 509 Controlled Cool (−21° C.) butan-1-ol: 1% H₂0 No Solid 510 Evaporation butan-1-ol: 1% H₂0 Form II 511 Anti-Solvent (IPA) butan-1-ol: 1% H₂0 No Solid Addition Elevated Temperature 512 Anti-Solvent (IPA) butan-1-ol: 1% H₂0 No Solid Addition Ambient Temperature 513 Anti-Solvent (IPA) butan-1-ol: 1% H₂0 No Solid Addition (4° C.) 514 Anti-Solvent (IPA) butan-1-ol: 1% H₂0 No Solid Addition (−21° C.) 515 Anti-Solvent (Ethanol) butan-1-ol: 1% H₂0 No Solid Addition Ambient Temperature 516 Anti-Solvent (Ethanol) butan-1-ol: 1% H₂0 No Solid Addition (4° C.) 517 Anti-Solvent (Ethanol) butan-1-ol: 1% H₂0 No Solid Addition (−21° C.) 518 Temp. Cycling butan-1-ol: 3% H₂0 Form II 519 Controlled Cool (4° C.) butan-1-ol: 3% H₂0 No Solid 520 Controlled Cool (−21° C.) butan-1-ol: 3% H₂0 No Solid 521 Evaporation butan-1-ol: 3% H₂0 Form II 522 Anti-Solvent (IPA) butan-1-ol: 3% H₂0 No Solid Addition Elevated Temperature 523 Anti-Solvent (IPA) butan-1-ol: 3% H₂0 No Solid Addition Ambient Temperature 524 Anti-Solvent (IPA) butan-1-ol: 3% H₂0 No Solid Addition (4° C.) 525 Anti-Solvent (IPA) butan-1-ol: 3% H₂0 No Solid Addition (−21° C.) 526 Anti-Solvent (Ethanol) butan-1-ol: 3% H₂0 No Solid Addition Ambient Temperature 527 Anti-Solvent (Ethanol) butan-1-ol: 3% H₂0 No Solid Addition (4° C.) 528 Anti-Solvent (Ethanol) butan-1-ol: 3% H₂0 No Solid Addition (−21° C.) 529 Temp. Cycling butan-1-ol: 5% H₂0 Form II 530 Controlled Cool (4° C.) butan-1-ol: 5% H₂0 No Solid 531 Controlled Cool (−21° C.) butan-1-ol: 5% H₂0 No Solid 532 Evaporation butan-1-ol: 5% H₂0 Form II 533 Anti-Solvent (IPA) butan-1-ol: 5% H₂0 No Solid Addition Elevated Temperature 534 Anti-Solvent (IPA) butan-1-ol: 5% H₂0 Form II Addition Ambient Temperature 535 Anti-Solvent (IPA) butan-1-ol: 5% H₂0 No Solid Addition (4° C.) 536 Anti-Solvent (IPA) butan-1-ol: 5% H₂0 No Solid Addition (−21° C.) 537 Anti-Solvent (Ethanol) butan-1-ol: 5% H₂0 No Solid Addition Ambient Temperature 538 Anti-Solvent (Ethanol) butan-1-ol: 5% H₂0 No Solid Addition (4° C.) 539 Anti-Solvent (Ethanol) butan-1-ol: 5% H₂0 No Solid Addition (−21° C.) 540 Temp. Cycling 1,4-dioxane Form I 541 Evaporation 1,4-dioxane Form I/II 542 Anti-Solvent Addition 1,4-dioxane No Solid 543 Temp. Cycling 1-butanol Form I 544 Evaporation 1-butanol Form I/II 545 Anti-Solvent (Hexane) 1-butanol Form III Addition (4° C.) 546 Temp. Cycling ethanol Form I 547 Evaporation ethanol Form II 548 Anti-Solvent (Hexane) ethanol Form I Addition (4° C.) 549 Temp. Cycling acetone Form I 550 Evaporation acetone Form II 551 Anti-Solvent (Hexane) acetone Form III Addition (4° C.) 552 Temp. Cycling benzonitrile Form I 553 Evaporation benzonitrile Form II 554 Anti-Solvent (Hexane) benzonitrile Form II Addition (4° C.) 555 Temp. Cycling cyclohexane Form I 556 Evaporation cyclohexane Form II 557 Anti-Solvent (Hexane) cyclohexane No Solid Addition (4° C.) 558 Temp. Cycling DCM Form I 559 Evaporation DCM Form II 560 Anti-Solvent (Hexane) DCM Form III Addition (4° C.) 561 Temp. Cycling DMSO Form I 562 Evaporation DMSO Form II/II 563 Anti-Solvent (Hexane) DMSO No Solid/No Addition (4° C.) Solid 564 Temp. Cycling EtOAc Form I 565 Evaporation EtOAc Form II 566 Anti-Solvent (Hexane) EtOAc Form III Addition (4° C.) 567 Temp. Cycling Heptane Form I 568 Evaporation Heptane Form I/II 569 Anti-Solvent (Hexane) Heptane No Solid/No Addition (4° C.) Solid 570 Temp. Cycling IPA Form I 571 Evaporation IPA Form I/II 572 Anti-Solvent (Hexane) IPA No Solid Addition (4° C.) 573 Temp. Cycling IPA: Water (1%) Form I 574 Evaporation IPA: Water (1%) Form II 575 Anti-Solvent (Hexane) IPA: Water (1%) No Solid/No Addition (4° C.) Solid 576 Temp. Cycling MeCN Form I 577 Evaporation MeCN Form II 578 Anti-Solvent (Hexane) MeCN Form I/III Addition (4° C.) 579 Temp. Cycling MeCN: Water (1%) Form I 580 Evaporation MeCN: Water (1%) Form I/II 581 Anti-Solvent (Hexane) MeCN: Water (1%) No Solid Addition (4° C.) 582 Temp. Cycling MEK Form I 583 Evaporation MEK Form I/II 584 Anti-Solvent (Hexane) MEK Form III Addition (4° C.) 585 Temp. Cycling MeOAc Form I 586 Evaporation MeOAc Form II 587 Anti-Solvent (Hexane) MeOAc Form III Addition (4° C.) 588 Temp. Cycling MeOH Form I 589 Evaporation MeOH Form I/II 590 Anti-Solvent (Hexane) MeOH Form III Addition (4° C.) 591 Temp. Cycling MIBK Form I 592 Evaporation MIBK Form II 593 Anti-Solvent (Hexane) MIBK No Solid Addition (4° C.) 594 Temp. Cycling Nitromethane Form I 595 Evaporation Nitromethane Form II 596 Anti-Solvent (Hexane) Nitromethane Form I Addition (4° C.) 597 Temp. Cycling TBME Form I 598 Evaporation TBME Form II 599 Anti-Solvent (Hexane) TBME Form I Addition (4° C.) 600 Temp. Cycling THF Form I 601 Evaporation THF Form II 602 Anti-Solvent (Hexane) THF Form I/III Addition (4° C.) 603 Temp. Cycling THF: water (1%) Form I 604 Evaporation THF: water (1%) Form I/II 605 Anti-Solvent (Hexane) THF: water (1%) No Solid Addition (4° C.) 606 Temp. Cycling toluene Form I 607 Evaporation toluene Form II 608 Anti-Solvent (Hexane) toluene Form III Addition (4° C.) 609 Temp. Cycling water No Solid 610 Evaporation water Form I/II 611 Anti-Solvent (Hexane) water Form III Addition (4° C.)

Example 2 Intrinsic Dissolution Studies

The intrinsic dissolution rates for Forms I, II, and III were measured at pH conditions of 1.0, 4.5 and 6.7. The results are reproduced below in TABLE 6. In each case, complete dissolution was achieved in less than 3 minutes. Surprisingly, a pH dependence was observed for Form II; with the intrinsic dissolution rate increasing with the pH. In contrast, Forms I and III appear to dissolve at rates independent of pH.

TABLE 6 Calculated Intrinsic Dissolution Rates (mg/cm²/s) 1.0 4.5 6.7 Form I 0.41 0.44 0.37 Form II 0.26 0.34 0.62 Form III 0.49 0.44 0.45

Example 3 Solubility Studies

The solubility of L-ornithine phenyl acetate was approximated according to methods disclosed above. 24 solvents systems were tested: 1,4 dioxane, 1-butanol, ethanol, acetone, benzonitrile, cyclohexane, DCM, DMSO, EtOAc, Heptane, IPA, IPA (1% H₂O), MeCN, MeCn (1% H₂O), MEK, MeOAc, methanol, MIBK, Nitromethane, THF, THF (1% H₂O), Toluene and water. L-ornithine phenyl acetate exhibited a solubility in water, whereas L-ornithine phenyl acetate was substantially insoluble in the remaining solvent systems.

Slurries of L-ornithine phenyl acetate in water were also prepared and the slurry was filtered. The filtrate concentration was analyzed by HPLC, and the results show the solubility of L-ornithine phenyl acetate to be about 1.072 mg/mL.

HPLC determinations of solubility were also completed for five solvents: ethanol, acetone, methanol, DMSO and IPA. These results are summarized in TABLE 7.

TABLE 7 HPLC Solubility Determinations Solubility Solvent (mg/mL) Peak Area Comments EtOH <0.0033 N/A Small peak Acetone 0 0 API content beyond the lower limit of quantification (LLOQ) MeOH 0.0033 1906.75 Resolved peak DMSO >0.0033 N/A Shoulder on DMSO peak IPA 0 0 API content beyond the LLOQ

These results indicate that both acetone and IPA are suitable as anti-solvents for precipitating L-ornithine phenyl acetate. In contrast, solvents with measurable solubility are less favorable for precipitating crystalline forms of L-ornithine phenyl acetate.

Finally, the solubility of L-ornithine phenyl acetate was determined in various mixtures of IPA and water using HPLC. The results are shown in TABLE 8.

TABLE 8 HPLC Solubility Determinations (IPA/Water) % IPA Peak Area Solubility (mg/mL) 100 0 0 90 295 0.0054 80 2634 0.0455 70 8340 0.1433

Example 4 Small-Scale Batch Process to Produce L-Ornithine Phenyl Acetate

About 8.4 g (0.049 moles) of L-ornithine HCl was dissolved in 42 mL H₂O and, separately, about 11.4 g of silver benzoate was dissolved in 57 mL DMSO. Subsequently, the silver benzoate solution was added to the L-ornithine HCl solution. Combining the two mixtures resulted in an immediate, exothermic precipitation of a creamy white solid (AgCl). The solid was removed by vacuum filtration and retaining the filtrate (L-ornithine benzoate in solution). 200 mL of IPA was added to the filtrate and the mixture was cooled to 4° C. A crystalline solid precipitated after about 3 hours (L-ornithine benzoate) which was isolated by vacuum filtration. Yield: 60%

7.6 g (0.03 moles) of the L-ornithine benzoate was dissolved in 38 mL H₂O and about 4.4 g of sodium phenyl acetate was dissolved 22 mL H2O. Subsequently, the sodium phenyl acetate solution was added to the L-ornithine benzoate solution and left to stir for about 10 minutes About 240 mL of IPA (8:2 IPA:H₂O) was added and the solution stirred for 30 minutes before cooling to 4° C. A crystalline solid precipitated after about 3 hrs at 4° C. (L-ornithine phenyl acetate). The precipitate was isolated by vacuum filtration and washed with 48-144 mL of IPA. Yield: 57%

Example 5 Large-Scale Batch Process to Produce L-Ornithine Phenyl Acetate

Two separate batch of L-ornithine phenyl acetate were prepared as follows:

About 75 Kg of L-Ornithine monohydrochloride was dissolved in 227 kg of water. To the resulting solution was added 102 Kg of silver benzoate dissolved in 266 kg of DMSO at room temperature within 2 hours. Initially, a strong exothermy was observed and the silver chloride precipitated. The receiver containing the solution was then washed with 14 Kg of DMSO that was added to the reaction mass. In order to remove the silver chloride formed, the reaction mass was filtered over a lens filter prepared with 10 kg of Celite and a GAF filter of 1 mm. After filtration, the filter was washed with an additional 75 kg of water. The reaction mass was then heated at 35±2° C. and 80 kg of sodium phenyl acetate was added. At this point the reaction mass was stirred at 35±2° C. for at least 30 minutes.

In order to precipitate the final API, 353 kg of isopropyl alcohol was added to the reaction mass. The reaction mass was then cooled to 0±3° C. within 6 hours, stirred for 1 hour and then the product isolated in a centrifuge.

About 86 kg of finished wet produce was obtained. The product was then dried at 40±5° C. for about 6.5 to 8 hours to provide about 75 kg of L-ornithine phenyl acetate. Yield: 63.25. TABLE 9 summarizes measurements relating to the final product.

TABLE 9 Analytical Results for Large-scale Batch Process Test Batch 1 Batch 2 Purity 98.80% 98.74% Benzoate  0.17%  0.14% Silver 28 ppm 157 ppm Chloride 0.006% 0.005% Sodium  7 ppm  26 ppm Total Impurities  0.17%  0.14% Physical Form Form II Form II

Example 6 Reducing Silver Content in L-Ornithine Phenyl Acetate

Batch 2 from Example 5 exhibited high amounts of silver (157 ppm), and therefore procedures were tested for reducing the silver content. Nine trials were completed; each generally including dissolving about 20 g of L-ornithine phenyl acetate from Batch 2 into 1.9 parts water, and then subsequently adding 10.8 parts IPA. A crystalline form was isolated at 0° C. by filtration.

For four trials, 8.0 mg or 80 mg of heavy metal scavengers SMOPEX 102 or SMOPEX 112 were added to the aqueous solution and stirred for 2 hours. The scavengers failed to reduce the silver content below 126 ppm. Meanwhile, another trial applied the general conditions disclosed above and reduced the silver content to 179 ppm. In still another trial, the L-ornithine phenyl acetate was slurried in a solution of IPA, rather than crystallized; however this trial also failed to reduce the silver content below 144 ppm.

The last three trials included adding diluted HCl to the solution to precipitate remaining amount of silver as AgCl. The precipitate was then removed by filtration before The three trials included adding: (1) 1.0 g of 0.33% HCl at 20° C.; (2) 1.0 g of 0.33% HCl at 30° C.; and (3) 0.1 g of 3.3% HCl at 20° C. The three trials reduced the silver content to 30 ppm, 42 ppm, and 33 ppm, respectively, and each trial yielding greater than 90% L-ornithine phenyl acetate. Accordingly, the addition of HCl was effective in reducing the amount of residual silver.

Example 6 Process for Preparing L-Ornithine Phenyl Acetate without an Intermediate Salt

As a general procedure, L-ornithine hydrochloride was suspended in a solvent. After that the reaction mass was heated and a base, sodium methoxide, was added. NaCl formed and was removed from the system by filtration. The reaction mass was cooled and a molar equivalent of phenyl acetic acid was added to the reaction mass in order to form L-ornithine phenyl acetate. The final product was isolated, washed and dried. A summary of the trial for this process is provided in TABLE 10.

TABLE 10 Process Trials Trial Base Eq. of Base Solvent 1 NaOMe 21% in MeOH 1.0 eq. MeOH 2 NaOMe 21% in MeOH 0.95 eq.  IPA 3 NaOMe 21% in EtOH 1.0 eq. EtOH 4 NaOMe 21% in MeOH 1.0 eq. MeOH 5 NaOMe 21% in MeOH 1.0 eq. MeOH w/ IPA for precipitation 6 NaOMe 21% in MeOH 1.0 eq. Acetonitrile 7 NaOMe 21% in MeOH 1.0 eq. Water/IPA 8 NaOMe 21% in MeOH 1.0 eq. Water/IPA 9 NaOMe 21% in MeOH 1.0 eq. n-butanol

The resulting L-ornithine phenyl acetate was found to exhibit high amounts of chloride (at least about 1% by weight), and presumably include similar amounts of sodium. The yields were about 50% for Trials 2, 4, and 5.

Example 7 Thermal Stability Studies of Forms I, II, and III

Samples of Forms I, II and III were stored at increased temperatures and designated conditions as outlined in TABLE 11. The vacuum applied 600 psi to achieve the reduced pressure. The final compositions were tested by XRPD, NMR, IR and HPLC to determine any changes to the material.

Most notably, Form III does not transition to Form II under vacuum at 120° C., but rather exhibits greater chemical degradation compared to Forms I and II under these conditions. Meanwhile, Form III converts to Form II and exhibits substantial chemical degradation at 120° C. without a vacuum.

Form I converted to Form II in all the trials, but most interestingly, Form I exhibits substantial chemical degradation at 120° C. without a vacuum. Thus, the conversion from Form I does not exhibit the same chemical stability as Form II, which is surprising considering the material readily converts to Form II.

Form II was stable and did not chemically degrade in all of the trials. Thus, Form II is the most stable. Meanwhile, Form III is more stable than Form I, but both forms exhibit substantial chemical degradation at 120° C. without a vacuum.

TABLE 11 Thermal Stability Trials Initial Trial Form Temperature Condition Period Results 1 Form I 80° C. no vacuum  7 days Form II, no degradation 2 Form I 80° C. vacuum  7 days Form II, no degradation 3 Form I 80° C. no vacuum 14 days Form II, no degradation 4 Form I 80° C. vacuum 14 days Form II, no degradation 5 Form II 80° C. no vacuum  7 days Form II, no degradation 6 Form II 80° C. vacuum  7 days Form II, no degradation 7 Form II 80° C. no vacuum 14 days Form II, no degradation 8 Form II 80° C. vacuum 14 days Form II, no degradation 5 Form III 80° C. no vacuum  7 days Form III, no degradation 5 Form III 80° C. no vacuum 14 days Form III, no degradation 6 Form I 120° C. no vacuum  7 days Form II (>96% API) 7 Form I 120° C. vacuum  7 days Form II (>99.9% API) 8 Form I 120° C. no vacuum 14 days Form II (37% API) 9 Form I 120° C. vacuum 14 days Form II (>96% API) 8 Form II 120° C. no vacuum  7 days Form II (98.6% API) 9 Form II 120° C. vacuum  7 days Form II (98.7% API) 10 Form II 120° C. no vacuum 14 days Form II (>95% API) 11 Form II 120° C. vacuum 14 days Form II (>95% API) 10 Form III 120° C. no vacuum  7 days Form II (<30% API) 11 Form III 120° C. vacuum  7 days Form III (>95% API) 12 Form III 120° C. no vacuum 14 days Form II (<30% API) 14 Form III 120° C. vacuum 14 days Form III (88.8% API)

HPLC results for the trials exhibiting chemical degradation (e.g., Trial 10 from TABLE 11) are summarized in TABLE 12. Each degraded material exhibits common peaks at relative retention times (RRT) of 1.9, 2.2, 2.4, and 2.7, which suggests a common degradation pathway for different forms.

TABLE 12 HPLC Results for Degraded Samples Main Peak Retention Time Degradation/Impuirty (min) Peak(s) HPLC Form Timepoint Retention % Peak Retention % Peak ID Sample ID Tested Stability Test (day) Time (min) Area Time (min) Area 39 W00045/45/3 III 120° C. ambient 7 2.857 35.786 6.763 6.103 pressure 7.582 45.161 42 W00045/45/6 III 120° C. under vacuum 7 2.787 88.885 7.598 9.389 (ca. 600 psi) 51 W00045/45/1 I 120° C. ambient 14 3.499 37.826 6.766 3.948 pressure 7.569 42.525 9.707 3.628 53 W00045/45/3 III 120° C. ambient 14 3.476 30.394 6.763 5.975 pressure 7.583 56.459 56 W00045/45/6 III 120° C. under vacuum 14 3.400 87.389 7.555 11.500 (ca. 600 psi)

Example 8 Oxygen Stability Studies of Forms I, II, and III

Samples of Forms I, II and III were stored in 100% oxygen environments for 7 or 14 days and analyzed by NMR and IR. The results establish that Forms I and II show no signs of degradation after 14 days. Only IR results were completed for Form III at 7 days, and these results confirm there was no significant degradation. TLC results for all samples indicated a single spot with similar R_(f) values.

Example 9 UV Stability Studies of Forms I, II, and III

Samples of Forms I, II and III were exposed to ultraviolet (UV) radiation for 7 or 14 days. A CAMAG universal UV Lampe applied radiation to the samples with setting of 254 mμ. NMR and IR results show no degradation of Forms I and II after 14 days. Similarly, Form III exhibits no degradation after 7 days as determined by NMR and IR. TLC results for all samples indicated a single spot with similar R_(f) values.

Example 10 pH Stability Studies of Forms I, II, and III

A slurry of Forms I, II and III were formed with water and the pH value adjusted to either 1.0, 4.0, 7.0, 10.0, and 13.2. The slurries were stored for 7 or 14 days, and subsequently the solids were removed by filtration. Form I converted to Form II in all of the samples. NMR and IR results show Forms I and II did not degrade after 14 days in the varied pHs, and similarly HPLC results show about 98% purity or more for these samples. Form III also exhibited no degradation after 7 days according to NMR and IR results. HPLC tests show about 95% purity or more; however IR results show Form III converted to Form II over the 7-day test. TLC results for all samples indicated a single spot with similar R_(f) values.

Example 11 Compression Studies of Forms I, II, and III

Samples of Forms I, II and III were subjected to 3 tons of force using a Moore Hydraulic Press for about 90 minutes. The resultant tablet's mass, diameter and thickness were measured to determine the density. The tablets were also analyzed by NMR and IR. Form I transitioned to a composition of Form II with a density of 1.197 kg/m³. Form II did not exhibit a transition and had a final density of 1.001 kg/m³. Finally, Form III did not exhibit a transition and had a final density of 1.078 kg/m³.

Example 12 Process for Producing L-Ornithine Phenyl Acetate Via an Acetate Intermediate

Dissolve 25 mg of L-ornithine HCl 5 vols of H₂O, and then add excess acetic acid (about 5 vols) to form a slurry. Subject the slurry to temperature cycling between 25° and 40° C. every 4 hours for about 3 days. Add 1 equivalent of phenylacetic acid (with respect to L-ornithine) and stir for about 4-6 hrs (possibly heat). Use IPA as an anti-solvent, add enough to obtain a ratio of 70:30 (IPA:H₂O). Isolate by vacuum filtration and dry for about 4-8 hrs at 80° C. to remove any residual acetic acid. 

What is claimed is:
 1. A composition comprising a crystalline form of L-ornithine phenyl acetate, wherein said crystalline form exhibits an X-ray powder diffraction pattern comprising at least three characteristic peaks, wherein said characteristic peaks are selected from the group consisting of peaks at approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ.
 2. The composition of claim 1, wherein said crystalline form exhibits an X-ray powder diffraction pattern comprising characteristic peaks at approximately 5.8°, 14.1°, 18.6°, 19.4°, 22.3° and 24.8° 2θ.
 3. The composition of claim 1, wherein said crystalline form is characterized by differential scanning calorimetry as comprising an endotherm at about 40° C.
 4. The composition of claim 3, further comprising a melting point at about 203° C.
 5. The composition of claim 1, wherein said crystalline form exhibits an X-ray powder diffraction pattern substantially the same as FIG.
 11. 6. The composition of claim 1, wherein said crystalline form is anhydrous.
 7. A method of treating or ameliorating hyperammonemia in a subject by orally administering a therapeutically effective amount of the crystalline form of claim
 1. 8. The method of claim 7, wherein said crystalline form is administered from 1 to 3 times daily.
 9. The method of claim 7, wherein the therapeutically effective amount is in the range of about 500 mg to about 50 g.
 10. A method comprising dissolving the composition of claim 1 in an aqueous solution.
 11. The method of claim 10, further comprising administering the aqueous solution to a subject.
 12. The method of claim 11, wherein the aqueous solution comprises at least about 25 mg/mL of L-ornithine phenyl acetate.
 13. The method of claim 11, wherein the subject is a human.
 14. A method of compressing L-ornithine phenyl acetate, the method comprising applying pressure to a metastable form of L-ornithine phenyl acetate to induce a phase change, wherein the metastable form exhibits an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 4.9°, 17.4, 13.2°, 20.8° and 24.4° 2θ.
 15. The method of claim 14, wherein the pressure is applied for a predetermined time.
 16. The method of claim 14, wherein the predetermined time is about 1 second or less.
 17. The method of claim 14, wherein the pressure is at least about 500 psi.
 18. The method of claim 14, wherein the phase change yields a composition having a density in the range of about 1.1 to about 1.3 kg/m³ after applying the pressure.
 19. The method of claim 14, wherein the phase change yields a composition exhibiting an X-ray powder diffraction pattern comprising at least one characteristic peak, wherein said characteristic peak is selected from the group consisting of approximately 6.0°, 13.9°, 14.8°, 17.1°, 17.8° and 24.1° 2θ. 